Environmentally friendly refrigerant compositions having low flammability and low GWP

ABSTRACT

A refrigerant composition includes R-125 (pentafluoroethane), R-134a (1,1,1,2-tetrafluoroethane), R-32 (difluoromethane), R-227ea (1,1,1,2,3,3,3-heptafluoropropane), R-152a (1,1-difluoroethane), CO 2  and R-1234ze (1,3,3,3-tetrafluoropropene). In one exemplary embodiment, the refrigerant includes 18.5-20.5 wt % R-125, about 9-11 wt % R-134a, about 20-22 wt % R-32, about 3-5 wt % R-227ea, about 2.5-4.5 wt % R-152a, about 1-3 wt % CO 2  and about 39-41 wt % R-1234ze. Formulating with reclaimed material lowers the global warming potential to about 400 to about 750.

This application is a continuation-in-parts of application Ser. No. 17/236,354, filed Apr. 21, 2021, now U.S. Pat. No. 11,208,583, the entirety of which is incorporated by reference.

FIELD OF DISCLOSURE

The present disclosure relates generally to environmentally friendly refrigerant compositions that include pentafluoroethane, 1,1,1,2-tetrafluoroethane, difluoromethane, 1,1,1,2,3,3,3-heptafluoropropane, 1,1-difluoroethane, CO₂ and 1,3,3,3-tetrafluoropropene.

BACKGROUND

Refrigeration and air conditioning equipment frequently employ refrigerants to remove heat from a conditioned space. A refrigerant is a fluid used for heat transfer in a refrigerating system, which absorbs heat at a low temperature and a low pressure of the fluid and rejects heat at a higher temperature and a higher pressure of the fluid, usually involving changes of the state of the fluid.

Since the 1930s, R-12 (CCl₂F₂) and R-22 (CHClF₂) have been commonly used as refrigerants in refrigeration and air conditioning equipment. R-12 is a chlorofluorocarbon (CFC) refrigerant and R-22 is a hydrochlorofluorocarbon (HCFC) refrigerant. The release of CFC and HCFC refrigerants into the atmosphere has been found to deplete the Earth's protective ozone layer and contribute to climate change. The United States signed the Montreal Protocol on Substances that Deplete the Ozone Layer in 1987 and ultimately established proper refrigerant management procedures and a phase-out schedule that would ban the production and import of R-12 in 1996 and R-22 in 2020.

In response to the Montreal Protocol on Substances that Deplete the Ozone Layer, a non-ozone depleting refrigerant known as R-410A was developed in 1991. R-410A is a hydrofluorocarbon (HFC) refrigerant used primarily in residential and light commercial comfort cooling applications. Over the past decade, approximately 50 million pounds of R-410A was introduced into new and existing equipment each year.

HFC refrigerants released into the atmosphere have been found to contribute to global warming and climate change. In 2020, the US passed the American Innovation and Manufacturing (AIM) Act which gave the US Environmental Protection Agency (EPA) authority to establish a schedule to phasedown HFC refrigerants and a requirement to recover, reclaim, and reuse, or destroy, HFC refrigerants contained within equipment being repaired or taken out of service. Beginning in 2022, the phasedown schedule takes into account each refrigerant's Global Warming Potential (GWP) and gradually moves toward a cap on the consumption and production of HFC refrigerants equal to 15% of baseline (average annual production and consumption from 2011 to 2013) in 2036 and beyond. Starting in 2023, California Air Resources Board (CARB) has proposed regulations to reduce HFC emissions by requiring new air conditioning equipment to contain either R-410A refrigerant made up of 10% to 15% reclaimed R-410A or a refrigerant with a GWP rating of 750 or less.

As the supply of R-410A falls below demand and CARB regulations come into existence, servicing R-410A equipment will rely on R-410A substitutes, reclaimed R-410A, and declining stockpiles of R-410A refrigerant. A low-GWP substitute for R-410A will be needed to service the existing installed equipment base and provide a solution to reuse, as feedstock, HFC refrigerants recovered from R-410A equipment. The disclosed formulation solves both of these challenges.

Another widely used refrigerant is R-404A, which was designed as a replacement for R-22. It is used in commercial refrigerator equipment for low and medium temperature ranges. Its properties make it suitable for use in display cases, refrigerated vehicles, ice makers, and other applications. R-404A has a global warming potential (GWP) of 3920. This high GWP makes it unsuitable for further use in drop-in applications.

As of 2020, HFCs (including R-404A, R-134a and R-410A) are being superseded: with residential air-conditioning systems using R-32 or R-600a (isobutane); car air-conditioning systems using R-1234yf; chillers for commercial refrigeration; air conditioning using R-1234ze; and, commercial refrigeration using CO₂ (R-744). However, there is still a need for fluorinated hydrocarbon refrigerants having a low GWP.

On May 3, 2021, the EPA proposed a rule to slash the use of a potent climate-warming gas commonly used in refrigerators and air conditioners by 85% over the next 15 years, a move it said will play a big part in U.S. plans to halve its greenhouse gas emissions this decade. The proposal to curb the use of hydrofluorocarbons (HFCs) would keep the equivalent of 900 million tons of carbon dioxide emissions from reaching the atmosphere over that period, it said, a climate impact similar to preventing the combustion of a trillion tons of coal. The proposal would set annual “allocations” for each U.S. HFC producer and importer that gradually decline over time. It arises from a law passed by Congress in December 2020 that directed the EPA to issue regulations phasing down HFC production and imports.

The Background section of this document is provided to place embodiments of the present disclosure in technological and operational context, to assist those of skill in the art in understanding their scope and utility. Unless explicitly identified as such, no statement herein is admitted to be prior art merely by its inclusion in the Background section.

SUMMARY

The following presents a simplified summary of the disclosure in order to provide a basic understanding to those of skill in the art. This summary is not an extensive overview of the disclosure and is not intended to identify key/critical elements of embodiments of the disclosure or to delineate the scope of the disclosure. The sole purpose of this summary is to present some concepts disclosed herein in a simplified form as a prelude to the more detailed description that is presented later.

Briefly described, an embodiment of the disclosure relates to a refrigerant composition that includes R-125 (pentafluoroethane), R-134a (1,1,1,2-tetrafluoroethane), R-32 (difluoromethane), R-227ea (1,1,1,2,3,3,3-heptafluoropropane), R-152a (1,1-difluoroethane), CO₂ and R-1234ze (1,3,3,3-tetrafluoropropene). The formulations of the disclosure yield properties that make them excellent drop-in replacements for R-410A, R-404A and R-448A.

In one embodiment, the disclosure pertains to a refrigerant composition that includes about 14-16 wt % R-125, about 14-16 wt % R-134a, about 25-27 wt % R-32, about 3-5 wt % R-227ea, about 2-4 wt % R-152a, about 6-8 wt % CO₂ and about 29-31 wt % R-1234ze.

In one embodiment, the disclosure pertains to a refrigerant composition that includes about 15 wt % R-125, about 15 wt % R-134a, about 26 wt % R-32, about 4 wt % R-227ea, about 3 wt % R-152a, about 5 wt % CO₂ and about 30 wt % R-1234ze.

In another embodiment, the disclosure pertains to a refrigerant composition that includes about 14-16 wt % R-125, about 14-16 wt % R-134a, about 25-27 wt % R-32, about 3-5% HFC-227ea, about 2-4 wt % DME (dimethyl ether), about 6-8 wt % CO₂, and about 29-31 wt % R-1234ze.

In another embodiment, the refrigerant composition has a low GWP of about 1000 to 1100, or about 1048. The refrigerant composition can also have a GWP of about 1000 to about 1200.

In another embodiment, the refrigerant has a pressure of about 181 psi at 70° F. In another embodiment, at least part of the R-134a is reclaimed R-134a. In another embodiment, at least part of the R-125 is reclaimed R-125. In another embodiment, at least part of the R-32 is reclaimed R-32. In another embodiment, at least part of the R-227ea is recycled R-227ea. In another embodiment, at least part of the R-32 is reclaimed R-32. In another embodiment, at least part of the R-152a is reclaimed R-152a.

In the disclosure, adding up to 30 wt % reclaimed material yields a GWP of about 400-750. When the refrigerant composition contains about 10 wt % reclaimed R-410A or R-404A, this yields a global warming potential of about 630, or when the refrigerant composition contains about 10 wt % reclaimed R-407C, the global warming potential is about 487.

In another embodiment, the refrigerant composition has a liquid phase pressure of about 222 psia at 70° F., a vapor phase pressure of about 139 psia at 70° F., a liquid phase density of about 1.10 g/cm³ at 70° F., a vapor phase density of about 0.037 g/cm³ at 70° F., a liquid phase enthalpy of about 0.2323 kJ/g at 70° F., a vapor phase enthalpy of about 0.4283 kJ/g at 70° F., a liquid phase entropy of about 6.177×10⁻⁴ kJ/gR at 70° F. and a vapor phase entropy of about 9.988×10⁻⁴ kJ/gR at 70° F.

In another embodiment, the refrigerant composition has low flammability.

In another embodiment, a method for manufacturing a refrigerant includes charging a vessel with about 14-16 wt % R-125, about 14-16 wt % R-134a, about 25-27 wt % R-32, about 3-5 wt % R-227ea, about 2-4 wt % R-152a, about 6-8 wt % CO₂ and about 29-31 wt % R-1234ze. The CO₂ may be injected into the vessel last.

In another embodiment, a method for manufacturing a refrigerant includes charging a vessel with about 15 wt % R-125, about 15 wt % R-134a, about 26 wt % R-32, about 7 wt % CO₂ and about 30 wt % R-1234ze.

In another embodiment, the disclosure pertains to a refrigerant composition that includes about 18.5-20.5 wt % R-125, about 9-11 wt % R-134a, about 20-22 wt % R-32, about 3-5 wt % R-227ea, about 2.5-4.5 wt % R-152a, about 1-3 wt % CO₂ and about 39-41 wt % R-1234ze. The formulation can also be 19.5 wt % R-125, about 10 wt % R-134a, about 21 wt % R-32, about 4 wt % R-227ea, about 3.5 wt % R-152a, about 2 wt % CO₂ and about 40 wt % R-1234ze.

In an embodiment, the refrigerant composition has a liquid phase pressure of about 167 psia at 70° F., a vapor phase pressure of about 117 psia at 70° F., a liquid phase enthalpy of about 0.2308 kJ/g at 70° F., a vapor phase enthalpy of about 0.4160 kJ/g at 70° F., a liquid phase entropy of about 6.150×10⁻⁴ kJ/gR at 70° F., a vapor phase entropy of about 9.723×10⁻⁴ kJ/gR at 70° F., a global warming potential of about 1000 to about 1200, and may contain at least partially reclaimed material to yield a global warming potential of about 400-750. The refrigerant composition may contain about 10 wt % reclaimed R-404A to yield a global warming potential of about 630. The refrigerant composition has low flammability.

In another embodiment, a refrigerant composition contains about 19-21 wt % R-125, about 7-9 wt % R-134a, about 21-23 wt % R-32, about 3-5 wt % R-227ea and about 38-40 wt % R-1234ze. The formulation can also be about 20 wt % R125, about 8 wt % R-134a, about 22 wt % R-32, about 4 wt % R-227ea and about 39 wt % R-1234ze. The composition may have a liquid phase pressure of about 140 at 70° F., has a global warming potential of about 1000 to about 1200 and contain at least partially reclaimed material to yield a global warming potential of about 400-750.

BRIEF DESCRIPTION OF THE DRAWINGS

The present disclosure will now be described more fully hereinafter with reference to the accompanying drawings, in which embodiments of the disclosure are shown. However, this disclosure should not be construed as limited to the embodiments set forth herein. Rather, these embodiments are provided so that this disclosure will be thorough and complete, and will fully convey the scope of the disclosure to those skilled in the art. Like numbers refer to like elements throughout.

FIG. 1 depicts the liquid phase pressure-temperature curve of the refrigerant compositions of the disclosure compared to R-410A.

FIG. 2 depicts the liquid phase pressure-temperature curve of Example 15 of the disclosure compared to R-404A.

FIG. 3 depicts vapor pressure-temperature curve of the refrigerant compositions of the disclosure compared to R-410A.

FIG. 4 depicts the vapor phase pressure-temperature curve of Example 15 of the disclosure compared to R-404A.

FIG. 5 depicts the liquid phase enthalpy curve of the refrigerant compositions of the disclosure compared to R-410A.

FIG. 6 depicts the liquid phase enthalpy curve of Example 15 of the disclosure compared to R-404A.

FIG. 7 depicts vapor phase enthalpy versus temperature for Example 1 compared to R-410A.

FIG. 8 depicts the vapor phase enthalpy curve of Example 15 of the disclosure compared to R-404A.

FIG. 9 depicts the liquid phase entropy curve of the refrigerant compositions of the disclosure compared to R-410A.

FIG. 10 depicts the liquid phase entropy curve of Example 15 of the disclosure compared to R-404A.

FIG. 11 depicts the vapor phase entropy curve of the refrigerant compositions of the disclosure compared to R-410A.

FIG. 12 depicts the vapor phase entropy curve of Example 15 of the disclosure compared to R-404A.

FIG. 13 depicts vapor pressure versus temperature for Example 1 compared to R-410A.

FIG. 14 depicts the liquid phase enthalpy curve of Example 1 compared to R-410A

FIG. 15 depicts the vapor phase enthalpy curve of Example 1 compared to R-410A

FIG. 16 is a block diagram of a method of manufacturing the refrigerant composition of the disclosure.

FIG. 17 is a block diagram of a method of filling an apparatus designed for R-410A with the refrigerant of the disclosure.

FIG. 18 is a phase diagram of CO₂.

DETAILED DESCRIPTION

For simplicity and illustrative purposes, the present disclosure is described by referring mainly to exemplary embodiments thereof. In the following description, numerous specific details are set forth in order to provide a thorough understanding of the present disclosure. However, it will be readily apparent to one of ordinary skill in the art that the present disclosure may be practiced without limitation to these specific details.

The disclosure relates to low GWP refrigerant mixtures that can replace high GWP refrigerants such as R-410A while yielding similar or superior refrigeration performance. All new home air conditioning units in North America use R-410A, also known as AZ-20, EcoFluor R-410, Forane 410A, Genetron R-410A, Puron, and Suva 410A. But this refrigerant will consequently be phased out. This is due to a continued focus on reducing compounds known to have an effect on the environment. R-410A is a zeotropic but near-azeotropic mixture of R-32 and R-125.

Another high GWP refrigerant that will be replaced in the coming years is R-404A. R-404A is a pseudo-azeotropic mixed refrigerant composed of the three ingredients R-125, R-134a, and R-143a. It was introduced in the mid-1990s as a replacement for ozone depleting refrigerants including CFCs (such as R-12 and R-502) and more recently as a replacement for HCFCs (such as R-22). In the supermarket sector it has become the dominant refrigerant across Europe for both chilled and frozen food refrigeration. It is also used widely in other commercial systems, for industrial refrigeration and for cold storage. It is still used in many new systems, even though there are other better refrigerants now available.

The disclosure includes a refrigerant composition of R-125, R-134a, R-32, R-227ea, R-152, CO₂ and R-1234ze that performs similar to R-410A. In one embodiment, the composition includes about 14-16 wt % R-125, about 14-16 wt % R-134a, about 25-27 wt % R-32, about 3-5 wt % R-227ea, about 2-4 wt % R-152a, about 6-8 wt % CO₂ and about 29-31 wt % R-1234ze. In another embodiment, the refrigerant composition includes about 15 wt % R-125, about 15 wt % R-134a, about 26 wt % R-32, about 4 wt % R-227ea, about 3 wt % R-152a, about 5 wt % CO₂ and about 29-31 wt % R-1234ze.

The compositions of the disclosure was developed from a formulation, which is about 14-18 wt % R-134a, about 14-18 wt % R-125, about 23-27 wt % R-32, about 2-4 wt % R-152a, about 6-8 wt % CO₂ and about 29-31 wt % R-1234ze. It was unexpectedly found that the addition of R-227ea, which acts as a fire retardant, unexpectedly reduces the flammability of the refrigerant composition while matching the properties and performance of R-410A. In an embodiment, it was found that R-152a could be replaced with DME to achieve similar refrigeration performance.

Refrigerant compositions suitable as a drop-in replacement for R-404A include R-125, R-134a, R-32, R-227ea, R-152a, CO₂ and R-1234ze. In one exemplary embodiment, the refrigerant includes about 18.5-20.5 wt % R-125, about 9-11 wt % R-134a, about 20-22 wt % R-32, about 3-5 wt % R-227ea, about 2.5-4.5 wt % R-152a, about 1-3 wt % CO₂ and about 39-41 wt % R-1234ze. More specifically, the composition can include about 19.5 wt % R-125, about 10 wt % R-134a, about 21 wt % R-32, about 4 wt % R-227ea, about 3.5 wt % R-152a, about 2 wt % CO₂, and about 40 wt % R-1234ze.

Refrigerant compositions of the disclosure are set forth in Examples 1-8. Examples 1-8 compared to the formulation for R-410A are tabulated in Table 1.

TABLE 1 Refrigerant Compositions Examples 1-8 of the Disclosure Compared to R-410A. Generic Name Product Ex. 1 Ex. 2 Ex. 3 Ex. 4 1,1,1,2- R-134a 15.00% 15.00% 17.00% 15.00% tetrafluoroethane pentafluoroethane R-125 15.00% 15.00% 15.00% 17.00% difluoromethane R-32 26.00% 24.00% 24.00% 24.00% 1,1,1,2,3,3,3- R-227ea  4.00%  4.00%  4.00%  4.00% heptafluoropropane 1,1-difluoroethane R-152a  3.00%  3.00%  3.00%  3.00% dimethyl ether R-E170  0.00%  0.00%  0.00%  0.00% (DME) CO₂ CO₂  7.00%  7.00%  7.00%  7.00% 1,3,3,3 - R- 30.00% 32.00% 30.00% 30.00% tetrafluoropropene 1234ze(E) TOTAL 100.0%  100.0%  100.0%  100.0%  Liquid 221.7 218.9 219.1 221.2 Phase Pressure at 70° F. (psia) GWP 1048 1034 1063 1104 Theo BP* −73.07 −72.85 −72.92 −73.34 (° F.) Generic Name Product Ex. 5 Ex. 6 Ex. 7 Ex. 8 R-410A 1,1,1,2 R-134a 15.00% 15.00% 15.00% 15.00%  0.00% tetrafluoroethane pentafluoroethane R-125 15.00% 15.00% 15.00% 15.00% 50.00% difluoromethane R-32 26.00% 21.00% 24.00% 26.00% 50.00% 1,1,1,2,3,3,3- R-227ea  4.50%  4.00%  4.00%  4.00%  0.00% heptafluoropropane 1,1-difluoroethane R-152a  2.50%  5.00%  5.00%  0.00%  0.00% dimethyl ether R-E170  0.00%  0.00%  0.00%  3.00%  0.00% (DME) CO₂ CO₂  7.00%  7.00%  7.00%  7.00%  0.00% 1,3,3,3- R- 30.00% 30.00% 30.00% 30.00%  0.00% tetrafluoropropene 1234ze(E) TOTAL 100.0%  100.0%  100.0%  100.0%  100.0%  Liquid 222.2 227.9 217.8 218.1 216.5 Phase Pressure at 70° F. (psia) GWP 1063 1017 1037 1044 2088 Theo BP* −73. 17 −77.34 −72.67 −72.44 −60.60 (°F.) *Calculated from REFPROP

TABLE 1A Refrigerant Compositions Examples 9-15 of the Disclosure Compared to R-404A. Generic Name Product Ex. 9 Ex. 10 Ex. 11 Ex. 12 1,1,1,2- R-134a     9.00%     8.00%     8.00%     8.00% tetrafluoroethane pentafluoroethane R-125    20.00%    20.00%    20.00%    18.00% difluoromethane R-32    22.00%    13.00%    21.00%    21.00% 1,1,1,2,3,3,3- R-227ea     4.00%     4.00%     4.00%     4.00% heptafluoropropane 1,1-difluoroethane R-152a     3.00%     3.00%     4.00%     5.00% 1,1,1- R-143a     0.00% 10.00%     0.00%     0.00% trifluoroethane CO₂ CO₂     2.00%     3.00%     2.00%     2.00% 1,3,3,3- R-1234ze(E)     40.0%     39.0%     41.0%     42.0% tetrafluoropropene TOTAL    100.0%    100.0%    100.0%    100.0% Liquid Phase 169.1 171.9 166.7 164.4 Pressure at 70° F. (psia) GWP 1110   1482   1090   1022   Theo BP* (° F.)  −56.00    −59.81    −55.49    −54.85  

TABLE 1A Refrigerant Compositions Examples 9-15 of the Disclosure Compared to R-404A. Generic Name Product Ex.13 Ex. 14 Ex. 15 R-404A 1,1,1,2- R-134a     9.00%     9.00%    10.00%     4.00% tetrafluoroethane pentafluoroethane R-125    18.00%    19.00%    19.50%    44.00% difluoromethane R-32    23.00%    22.00%    21.00%     0.00% 1,1,1,2,3,3,3- R-227ea     4.00%     4.00%     4.00%     0.00% heptafluoropropane 1,1-difluoroethane R-152a     3.00%     3.00%     3.50%     0.00% dimethyl ether (DME) R-E170     0.00%     0.00%     0.00%     0.00% CO₂ CO₂     2.00%     2.00%     2.00%     0.00% 1,3,3,3- R-1234ze(E)    41.00%    41.00%    40.00%     0.00% tetrafluoropropene 1,1,1- R143a     0.00%     0.00%     0.00%    52.00% trifluoroethane TOTAL    100.0%    100.0%    100.0%    100.0% Liquid 169.1 168.2 166.6 164.0 Phase Pressure at 70° F (psia) GWP 1047   1075   1101   3922   Theo BP* (° F)  −55.9   −55.77    −55.42    −51.19   *Calculated from REFPROP

The refrigerant formulations of the disclosure have a low Global Warming Potential (GWP) between 1000 and about 1100. In contrast, R-410A has a GWP of 2087.5, which is almost 2 times the GWP of the formulations of the disclosure. R-404A has a GWP of 3922, which is almost triple the GWP of the disclosures. It is notable that in 2014, the United States, Canada and Mexico proposed an amendment to the Montreal Protocol to reduce production and consumption of HFCs by 85% during the period 2016-2035. Having a low GWP weighs the amount of HFC consumption downwards.

Thermodynamic values for the formulations of the disclosure compared to R-410A and R-404A were evaluated using the REFPROP software from NIST.

The liquid and vapor phase pressures of Ex. 1 to 8 compared to R-410A and R-404A at 70° F. is shown in Table 2.

TABLE 2 70° F. Liquid and Vapor Phase Pressure, Enthalpy and Entropy of R-410A and R-404A Compared to Ex. 1 to 8 and 15 of the Disclosure. Liquid Phase Vapor Phase Liquid Phase Vapor Phase Liquid Phase Vapor Phase Pressure Pressure Enthalpy Enthalpy Entropy Entropy Material (psia) (psia) (kJ/g) (kJ/g) (kJ/gR) (kJ/gR) R-410A 216.5 215.8 0.2334 0.4259 6.197 × 10⁻⁴ 9.832 × 10⁻⁴ Ex. 1 221.7 139.1 0.2323 0.4283 6.177 × 10⁻⁴ 9.988 × 10⁻⁴ Ex. 2 218.9 135.2 0.2321 0.4260 6.173 × 10⁻⁴ 9.947 × 10⁻⁴ Ex. 3 219.1 135.9 0.2321 0.4263 6.174 × 10⁻⁴ 9.951 × 10⁻⁴ Ex. 4 221.2 137.5 0.2321 0.4250 6.173 × 10⁻⁴ 9.925 × 10⁻⁴ Ex. 5 222.2 139.4 0.2323 0.4273 6.176 × 10⁻⁴ 9.970 × 10⁻⁴ Ex. 6 227.9 137.5 0.2329 0.4264 6.189 × 10⁻⁴ 9.963 × 10⁻⁴ Ex. 7 217.8 134.8 0.2322 0.4285 6.177 × 10⁻⁴ 9.994 × 10⁻⁴ Ex. 8 218.1 134.2 0.2310 0.4322 7.056 × 10⁻⁴ 10.97 × 10⁻⁴ R-404A  164.01 162.1 0.2304 0.3752 6.142 × 10⁻⁴ 8.877 × 10⁻⁴

As can be seen, the correspondence of the Examples of the disclosure approximate that of R-410A and R-404A for liquid phase pressure, liquid phase enthalpy, vapor phase enthalpy, liquid phase entropy and vapor phase entropy.

The theoretical vapor pressure versus temperature relationship was calculated for Examples 1-8 of the disclosure compared to R-410A and R-404A. The results are in Table 3.

TABLE 3 Liquid Pressure Versus Temperature Relationship of Examples 1-8 of the Disclosure Compared to R-410A and R-404A. Ex. 1 Ex. 2 Ex. 3 Ex. 4 Ex. 5 Liquid Liquid Liquid Liquid Liquid Phase Phase Phase Phase Phase Temp. Pressure Pressure Pressure Pressure Pressure (° F.) (psia) (psia) (psia) (psia) (psia) −60 20.57 20.44 20.47 20.71 20.63 −55 23.25 23.09 23.12 23.38 23.31 −50 26.19 26.00 26.04 26.32 26.26 −45 29.41 29.19 29.23 29.54 29.48 −40 32.92 32.67 32.71 33.06 33.00 −35 36.74 36.45 36.49 36.89 36.83 −30 40.89 40.56 40.61 41.04 40.10 −25 45.39 45.01 45.06 45.54 45.51 −20 50.26 49.83 49.88 50.40 50.38 −15 55.51 55.02 55.07 55.65 55.64 −10 61.16 60.60 60.66 61.29 61.31 −5 67.23 66.60 66.66 67.35 67.39 0 73.74 73.03 73.10 73.85 73.92 5 80.70 79.91 79.98 80.80 80.90 10 88.15 87.27 87.34 88.23 88.36 15 96.09 95.11 95.19 96.15 96.32 20 104.5 103.5 103.5 104.6 104.8 25 113.5 112.3 112.4 113.5 113.8 30 123.1 121.7 121.8 123.1 123.4 35 133.2 131.7 131.8 133.1 133.5 40 143.9 142.3 142.4 143.8 144.2 45 155.2 153.5 153.6 155.1 155.6 50 167.2 165.2 165.4 167.0 167.6 55 179.8 177.7 177.8 179.5 180.2 60 193.1 190.7 190.9 192.7 193.5 65 207.0 204.5 204.7 206.6 207.5 70 221.7 218.9 219.1 221.2 222.2 75 237.1 234.1 234.3 236.5 237.6 80 253.2 250.0 250.2 252.6 253.8 85 270.1 266.6 266.9 269.4 270.7 90 287.8 284.0 284.3 286.9 288.4 95 306.3 302.2 302.5 305.3 307.0 100 325.6 321.2 321.6 324.5 326.3 105 345.8 341.0 341.4 344.5 346.5 110 366.8 361.7 362.1 365.3 367.5 115 388.6 383.1 383.6 387.0 389.4 120 411.4 405.5 406.0 409.6 412.2 125 435.0 428.7 429.2 433.0 435.8 Ex. 6 Ex. 7 Ex. 8 R-410A Ex. 15 R-404A Liquid Liquid Liquid Liquid Liquid Liquid Phase Phase Phase Phase Phase Phase Temp. Pressure Pressure Pressure Pressure Pressure Pressure (° F.) (psia) (psia) (psia) (psia) (psia) (psia) −60 22.71 20.33 20.25 14.95 13.03 11.56 −55 25.55 22.97 22.89 17.17 14.86 13.27 −50 28.67 25.87 25.78 19.55 16.89 15.17 −45 32.06 29.03 28.94 22.41 19.13 17.29 −40 35.76 32.49 32.40 25.45 21.59 19.62 −35 39.77 36.26 36.16 28.82 24.29 22.20 −30 44.11 40.34 40.24 32.52 27.25 25.03 −25 48.80 44.77 44.66 36.58 30.48 28.14 −20 53.86 49.55 49.45 41.03 34.00 31.53 −15 59.30 54.71 54.61 45.88 37.82 35.23 −10 65.14 60.27 60.17 51.17 41.97 39.26 −5 71.40 66.23 66.14 56.91 46.45 43.63 0 78.10 72.63 72.54 63.13 51.29 48.36 5 85.26 79.48 79.39 69.86 56.50 53.47 10 92.88 86.79 86.71 77.12 62.11 58.98 15 101.0 94.58 94.52 84.95 68.12 64.91 20 109.6 102.9 102.8 93.36 74.56 71.28 25 118.8 111.7 111.7 102.4 81.45 78.12 30 128.5 121.1 121.1 112.1 88.80 85.43 35 138.8 131.0 131.0 122.4 96.63 93.26 40 149.6 141.5 141.5 133.5 105.0 101.6 45 161.0 152.6 152.8 145.3 113.8 110.5 50 173.1 164.3 164.4 157.9 123.2 120.0 55 185.8 176.7 176.8 171.2 133.2 130.0 60 199.2 189.7 189.9 185.4 143.7 140.7 65 213.2 203.4 203.6 200.5 154.9 152.0 70 227.9 217.8 218.1 216.5 166.6 164.0 75 243.3 232.9 233.2 233.4 179.0 176.7 80 259.5 248.7 249.1 251.2 192.1 190.1 85 276.4 265.2 265.7 270.1 205.8 204.2 90 294.0 282.6 283.1 290.1 220.2 219.2 95 312.4 300.7 301.3 311.1 235.3 234.9 100 331.6 319.6 320.3 333.2 251.2 251.5 105 351.6 339.3 340.2 356.6 267.8 268.9 110 372.5 359.8 360.8 381.1 285.2 287.2 115 394.1 381.2 382.3 407.0 303.4 306.5 120 416.6 403.5 404.7 434.1 322.4 326.6 125 440.0 426.6 428.0 462.6 342.2 348.0

The results of Table 3 are presented graphically in FIG. 1. As can be seen, the correspondence of the liquid phase pressure to R-410A is very close over the entire range. The pressure is identical starting at about 70° F. up to about 100° F., indicating identical performance when used as a drop-in for an air conditioner.

The results for Ex. 15 compared to R-404A are presented graphically in FIG. 2. As can be seen, the correspondence is so close that the curves overlap.

Table 4 presents the vapor phase pressure versus temperature of R-410A and R-404A compared to Examples 1 to 8 of the disclosure.

TABLE 4 Vapor Pressure Versus Temperature Relationship of Examples 1-8 and 15 of the Disclosure Compared to R-410A and R-404A. Ex. 1 Ex. 2 Ex. 3 Ex. 4 Ex. 5 Vapor Vapor Vapor Vapor Vapor Phase Phase Phase Phase Phase Temp. Pressure Pressure Pressure Pressure Pressure (° F.) (psia) (psia) (psia) (psia) (psia) −60 7.057 6.787 6.840 6.950 7.063 −55 8.257 7.946 8.006 8.133 8.264 −50 9.617 9.258 9.328 9.473 9.625 −45 11.15 10.74 10.82 10.99 11.16 −40 12.87 12.41 12.50 12.69 12.89 −35 14.80 14.27 14.37 14.59 14.82 −30 16.95 16.35 16.47 16.71 16.97 −25 19.35 18.67 18.80 19.07 19.37 −20 22.00 21.24 21.38 21.70 22.02 −15 24.93 24.08 24.23 24.58 24.96 −10 28.15 27.20 27.38 27.77 28.19 −5 31.70 30.64 30.84 31.27 31.74 0 35.58 34.41 34.63 35.11 35.63 5 39.83 38.54 38.78 39.31 39.89 10 44.46 43.03 43.29 43.88 44.52 15 49.50 47.93 48.21 48.86 49.57 20 54.97 53.24 53.56 54.27 55.05 25 60.89 59.00 59.34 60.13 60.98 30 67.30 65.22 65.60 66.46 67.40 35 74.21 71.95 72.36 73.29 74.32 40 81.65 79.19 79.64 80.66 81.78 45 89.66 86.98 87.47 88.58 89.80 50 98.26 95.35 95.88 97.08 98.41 55 107.5 104.3 104.9 106.2 107.6 60 117.3 113.9 114.5 116.0 117.5 65 127.9 124.2 124.9 126.4 128.1 70 139.1 135.2 135.9 137.5 139.4 75 151.1 146.9 147.6 149.0 151.4 80 163.9 159.3 160.1 162.1 164.2 85 177.5 172.6 173.5 175.5 177.8 90 192.0 186.7 187.6 189.8 192.3 95 207.3 201.6 202.6 205.0 207.7 100 223.6 217.5 218.6 221.1 224.0 105 240.8 234.3 235.5 238.2 241.2 110 259.1 252.2 253.4 256.3 259.5 115 278.4 271.0 272.3 275.5 278.9 120 298.9 291.0 292.4 295.8 299.4 125 320.5 312.1 313.6 317.2 321.1 Ex. 6 Ex. 7 Ex. 8 R-410A Ex. 15 R-404A Vapor Vapor Vapor Vapor Vapor Vapor Phase Phase Phase Phase Phase Phase Temp. Pressure Pressure Pressure Pressure Pressure Pressure (° F.) (psia) (psia) (psia) (psia) (psia) (psia) −60 6.918 6.796 6.752 14.90 5.785 11.10 −55 8.098 7.954 7.903 17.10 6.779 12.77 −50 9.434 9.266 9.206 19.58 7.907 14.64 −45 10.94 10.75 10.68 22.32 9.181 16.71 −40 12.64 12.41 12.33 25.36 10.62 19.00 −35 14.54 14.27 14.18 28.71 12.22 21.53 −30 16.66 16.35 16.25 32.41 14.02 24.31 −25 19.01 18.66 18.55 36.45 16.02 27.36 −20 21.63 21.23 21.10 40.89 18.24 30.71 −15 24.52 24.06 23.92 45.72 20.69 34.35 −10 27.70 27.18 27.02 50.99 23.39 38.32 −5 31.2 30.61 30.43 56.71 26.37 42.63 0 35.04 34.37 34.18 62.91 29.63 47.31 5 39.23 38.49 38.27 69.62 33.20 52.36 10 43.80 42.97 42.73 76.86 37.10 57.81 15 48.78 47.85 47.59 84.66 41.34 63.69 20 54.19 53.15 52.86 93.05 45.95 70.00 25 60.04 58.89 58.58 102.1 50.95 76.77 30 66.38 65.10 64.76 111.7 56.35 84.03 35 73.21 71.81 71.44 122.0 62.19 91.79 40 80.58 79.03 78.63 133.1 68.47 100.1 45 88.50 86.80 86.36 144.8 75.24 108.9 50 97.01 95.14 94.67 157.3 82.50 118.3 55 106.1 104.1 103.6 170.7 90.29 128.3 60 115.9 113.7 113.1 184.8 98.63 138.9 65 126.3 123.9 123.3 199.8 107.5 150.2 70 137.50 134.8 134.2 215.8 117.1 162.1 75 149.4 146.5 145.8 232.6 127.2 174.8 80 162.1 158.9 158.2 250.5 138.0 188.1 85 175.5 172.1 171.4 269.3 149.5 202.2 90 189.9 186.2 185.4 289.2 161.7 217.1 95 205.1 201.1 200.2 310.2 174.6 232.8 100 221.2 216.9 216.0 332.3 188.4 249.3 105 238.3 233.6 232.7 355.6 202.9 266.8 110 256.5 251.0 250.4 380.1 218.3 285.1 115 275.7 270.2 269.2 405.9 234.6 304.3 120 296.0 290.1 289.0 433.0 251.8 324.6 125 317.6 311.2 310.0 461.5 269.9 345.9

The results of Table 4 are presented graphically in FIG. 3. As can be seen, the correspondence of the vapor phase pressure to R-410A is very close at the lower temperature ranges.

The results of Table 4 for Example 15 compared to R-404A are shown in FIG. 4. As can be seen, the correspondence improves as the temperature lowers.

Table 5 presents the liquid phase enthalpy versus temperature of R-410A and R-404A compared to Examples 1 to 8 and 15 of the disclosure.

TABLE 5 Liquid Phase Enthalpy Versus Temperature Relationship of Examples 1-8 and 15 of the Disclosure Compared to R-410A and R-404A. Ex. 1 Ex. 2 Ex. 3 Ex. 4 Ex. 5 Liquid Liquid Liquid Liquid Liquid Phase Phase Phase Phase Phase En- En- En- En- En- Temp. thalpy thalpy thalpy thalpy thalpy (° F.) (kJ/g) (kJ/g)) (kJ/g)) (kJ/g) (kJ/g) −60 0.1277 0.1281 0.1281 0.1282 0.1279 −55 0.1325 0.1319 0.1318 0.1319 0.1316 −50 0.1353 0.1357 0.1356 0.1357 0.1354 −45 0.1391 0.1395 0.1394 0.1400 0.1392 −40 0.1429 0.1433 0.1432 0.1433 0.1431 −35 0.1468 0.1471 0.1471 0.1471 0.1469 −30 0.1506 0.1509 0.1509 0.1510 0.1507 −25 0.1545 0.1548 0.1547 0.1548 0.1546 −20 0.1584 0.1586 0.1590 0.1587 0.1585 −15 0.1623 0.1625 0.1625 0.1625 0.1624 −10 0.1662 0.1664 0.1664 0.1664 0.1663 −5 0.1702 0.1703 0.1703 0.1703 0.1702 0 0.1741 0.1743 0.1743 0.1743 0.1742 5 0.1781 0.1782 0.1782 0.1782 0.1781 10 0.1821 0.1820 0.1822 0.1822 0.1821 15 0.1861 0.1862 0.1862 0.1862 0.1862 20 0.1902 0.1902 0.1902 0.1902 0.1902 25 0.1943 0.1943 0.1943 0.1943 0.1943 30 0.1984 0.1984 0.1984 0.1984 0.1984 35 0.2025 0.2025 0.2025 0.2025 0.2025 40 0.2066 0.2070 0.2066 0.2066 0.2066 45 0.2108 0.2108 0.2108 0.2108 0.2108 50 0.2151 0.2150 0.2150 0.2150 0.2150 55 0.2193 0.2192 0.2192 0.2192 0.2193 60 0.2236 0.2235 0.2235 0.2235 0.2236 65 0.2279 0.2278 0.2278 0.2278 0.2279 70 0.2323 0.2321 0.2321 0.2321 0.2323 75 0.2367 0.2370 0.2365 0.2365 0.2367 80 0.2412 0.2409 0.2410 0.2409 0.2411 85 0.2457 0.2454 0.2454 0.2454 0.2456 90 0.2503 0.2499 0.2500 0.2500 0.2502 95 0.2549 0.2545 0.2546 0.2545 0.2548 100 0.2596 0.2592 0.2592 0.2592 0.2595 105 0.2643 0.2639 0.2639 0.2639 0.2642 110 0.2692 0.2687 0.2687 0.2687 0.2690 115 0.2741 0.2735 0.2736 0.2736 0.2739 120 0.2790 0.2784 0.2785 0.2785 0.2799 125 0.2841 0.2835 0.2835 0.2836 0.2840 Ex. 6 Ex. 7 Ex. 8 R-410A Ex. 15 R-404A Liquid Liquid Liquid Liquid Liquid Liquid Phase Phase Phase Phase Phase Phase En- En- En- En- En- En- Temp. thalpy thalpy thalpy thalpy thalpy thalpy (° F.) (kJ/g) (kJ/g) (kJ/g) (kJ/g) (kJ/g) (kJ/g) −60 0.1266 0.1277 0.1251 0.1268 0.1309 0.1332 −55 0.1304 0.1315 0.1290 0.1306 0.1345 0.1367 −50 0.1343 0.1353 0.1328 0.1345 0.1381 0.1402 −45 0.1382 0.1391 0.1367 0.1383 0.1418 0.1436 −40 0.1420 0.1430 0.1406 0.1422 0.1454 0.1472 −35 0.1459 0.1468 0.1445 0.1460 0.1491 0.1507 −30 0.1498 0.1507 0.1484 0.1499 0.1528 0.1542 −25 0.1538 0.1545 0.1523 0.1538 0.1565 0.1578 −20 0.1577 0.1584 0.1562 0.1577 0.1602 0.1614 −15 0.1617 0.1623 0.1602 0.1617 0.1640 0.1650 −10 0.1657 0.1662 0.1641 0.1657 0.1677 0.1686 −5 0.1697 0.1708 0.1681 0.1697 0.1715 0.1722 0 0.1737 0.1741 0.1721 0.1737 0.1753 0.1759 5 0.1777 0.1781 0.1762 0.1777 0.1791 0.1796 10 0.1818 0.1821 0.1802 0.1818 0.1829 0.1833 15 0.1859 0.1861 0.1843 0.1858 0.1866 0.1871 20 0.1900 0.1902 0.1884 0.1900 0.1906 0.1908 25 0.1942 0.1943 0.1925 0.1941 0.1945 0.1946 30 0.1983 0.1984 0.1966 0.1983 0.1984 0.1985 35 0.2025 0.2025 0.2008 0.2025 0.2024 0.2023 40 0.2068 0.2067 0.2050 0.2068 0.2063 0.2062 45 0.2110 0.2109 0.2093 0.2111 0.2103 0.2102 50 0.2153 0.2150 0.2135 0.2155 0.2144 0.2141 55 0.2197 0.2193 0.2178 0.2199 0.2184 0.2181 60 0.2240 0.2236 0.2222 0.2243 0.2225 0.2222 65 0.2285 0.2279 0.2265 0.2288 0.2266 0.2263 70 0.2329 0.2323 0.2310 0.2334 0.2308 0.2304 75 0.2374 0.2367 0.2354 0.2380 0.2351 0.2346 80 0.2420 0.2411 0.2399 0.2427 0.2392 0.2389 85 0.2466 0.2456 0.2445 0.2475 0.2435 0.2432 90 0.2513 0.2502 0.2491 0.2523 0.2478 0.2475 95 0.2560 0.2548 0.2537 0.2572 0.2522 0.2520 100 0.2608 0.2595 0.2584 0.2622 0.2566 0.2565 105 0.2656 0.2642 0.2632 0.2674 0.2611 0.2611 110 0.2705 0.2690 0.2681 0.2726 0.2656 0.2658 115 0.2755 0.2739 0.2730 0.2780 0.2702 0.2706 120 0.2806 0.2788 0.2780 0.2836 0.2748 0.2756 125 0.2859 0.2839 0.2831 0.2893 0.2796 0.2807

The results of Table 5 are presented graphically in FIG. 5. As can be seen, the correspondence of the liquid phase enthalpy pressure to R-410A is very close over the entire temperature range.

The results for Example 15 compared to R-404A are presented graphically in FIG. 6. As can be seen, the correspondence is so close that the curves overlap.

Table 6 presents the vapor phase enthalpy versus temperature of R-410A and R-404A compared to Examples 1 to 8 and 15 of the disclosure.

TABLE 6 Vapor Phase Enthalpy Versus Temperature Relationship of Examples 1-8 and 15 of the Disclosure Compared to R-410A and R-404A. Ex. 1 Ex. 2 Ex. 3 Ex. 4 Ex. 5 Vapor Vapor Vapor Vapor Vapor Phase Phase Phase Phase Phase En- En- En- En- En- Temp. thalpy thalpy thalpy thalpy thalpy (° F.) (kJ/g) (kJ/g) (kJ/g) (kJ/g) (kJ/g) −60 0.3883 0.3854 0.3859 0.3847 0.3874 −55 0.3901 0.3872 0.3876 0.3864 0.3892 −50 0.3918 0.3889 0.3894 0.3882 0.3909 −45 0.3936 0.3907 0.3912 0.3899 0.3927 −40 0.3953 0.3925 0.3933 0.3917 0.3944 −35 0.3970 0.3942 0.3946 0.3934 0.3961 −30 0.3986 0.3959 0.3964 0.3951 0.3978 −25 0.4004 0.3976 0.3981 0.3968 0.3995 −20 0.4021 0.3993 0.3998 0.3985 0.4012 −15 0.4038 0.4010 0.4014 0.4002 0.4029 −10 0.4054 0.4027 0.4031 0.4018 0.4045 −5 0.4071 0.4043 0.4047 0.4035 0.4061 0 0.4087 0.4060 0.4064 0.4051 0.4077 5 0.4103 0.4076 0.4080 0.4067 0.4093 10 0.4118 0.4092 0.4095 0.4083 0.4109 15 0.4134 0.4107 0.4111 0.4098 0.4124 20 0.4149 0.4123 0.4126 0.4114 0.4139 25 0.4164 0.4138 0.4142 0.4129 0.4154 30 0.4179 0.4153 0.4156 0.4144 0.4169 35 0.4193 0.4168 0.4171 0.4160 0.4183 40 0.4207 0.4182 0.4185 0.4172 0.4197 45 0.4221 0.4196 0.4199 0.4186 0.4211 50 0.4234 0.4210 0.4213 0.4200 0.4224 55 0.4247 0.4223 0.4226 0.4213 0.4237 60 0.4259 0.4236 0.4239 0.4225 0.4251 65 0.4271 0.4249 0.4251 0.4238 0.4262 70 0.4283 0.4260 0.4263 0.4250 0.4273 75 0.4294 0.4272 0.4274 0.4261 0.4285 80 0.4305 0.4283 0.4285 0.4272 0.4295 85 0.4315 0.4293 0.4296 0.4282 0.4305 90 0.4324 0.4303 0.4306 0.4292 0.4315 95 0.4333 0.4312 0.4315 0.4301 0.4323 100 0.4341 0.4321 0.4323 0.4309 0.4331 105 0.4348 0.4329 0.4331 0.4317 0.4338 110 0.4354 0.4336 0.4338 0.4323 0.4345 115 0.4360 0.4342 0.4343 0.4329 0.4350 120 0.4364 0.4347 0.4348 0.4334 0.4355 125 0.4367 0.4351 0.4352 0.4337 0.4358 Ex. 6 Ex. 7 Ex. 8 R-410A Ex. 15 R-404A Vapor Vapor Vapor Vapor Vapor Vapor Phase Phase Phase Phase Phase Phase En- En- En- En- En- En- Temp. thalpy thalpy thalpy thalpy thalpy thalpy (° F.) (kJ/g) (kJ/g) (kJ/g) (kJ/g) (kJ/g) (kJ/g) −60 0.3845 0.3879 0.3910 0.3994 0.3737 0.3368 −55 0.3863 0.3897 0.3928 0.4009 0.3755 0.3385 −50 0.3881 0.3915 0.3946 0.4023 0.3773 0.3402 −45 0.3899 0.3932 0.3964 0.4037 0.3791 0.3419 −40 0.3917 0.3950 0.3982 0.4050 0.3808 0.3435 −35 0.3935 0.3967 0.3999 0.4064 0.3830 0.3452 −30 0.3953 0.3985 0.4017 0.4077 0.3844 0.3468 −25 0.3971 0.4002 0.4034 0.4090 0.3861 0.3485 −20 0.3988 0.4019 0.4051 0.4103 0.3879 0.3501 −15 0.4006 0.4036 0.4068 0.4115 0.3896 0.3517 −10 0.4023 0.4052 0.4085 0.4127 0.3913 0.3533 −5 0.4040 0.4069 0.4102 0.4139 0.3930 0.3549 0 0.4057 0.4085 0.4119 0.4150 0.3947 0.3564 5 0.4074 0.4101 0.4135 0.4161 0.3963 0.3579 10 0.4090 0.4122 0.4151 0.4172 0.3980 0.3595 15 0.4106 0.4133 0.4167 0.4182 0.3996 0.3610 20 0.4122 0.4148 0.4183 0.4192 0.4012 0.3624 25 0.4138 0.4163 0.4198 0.4201 0.4028 0.3639 30 0.4153 0.4178 0.4213 0.4210 0.4044 0.3653 35 0.4168 0.4193 0.4228 0.4218 0.4059 0.3666 40 0.4184 0.4207 0.4243 0.4226 0.4075 0.3680 45 0.4198 0.4221 0.4257 0.4233 0.4090 0.3693 50 0.4212 0.4235 0.4271 0.4240 0.4104 0.3706 55 0.4225 0.4250 0.4284 0.4246 0.4119 0.3718 60 0.4239 0.4261 0.4297 0.4251 0.4133 0.3730 65 0.4252 0.4273 0.4310 0.4255 0.4146 0.3741 70 0.4264 0.4285 0.4322 0.4259 0.4160 0.3752 75 0.4276 0.4297 0.4334 0.4261 0.4172 0.3762 80 0.4287 0.4308 0.4345 0.4263 0.4185 0.3771 85 0.4500 0.4318 0.4356 0.4263 0.4197 0.3780 90 0.4308 0.4328 0.4366 0.4262 0.4208 0.3788 95 0.4318 0.4337 0.4375 0.4260 0.4219 0.3795 100 0.4326 0.4346 0.4384 0.4257 0.4230 0.3800 105 0.4334 0.4354 0.4392 0.4251 0.4239 0.3805 110 0.4341 0.4360 0.4399 0.4244 0.4249 0.3809 115 0.4347 0.4367 0.4406 0.4235 0.4257 0.3811 120 0.4352 0.4372 0.4411 0.4223 0.4264 0.3811 125 0.4356 0.4375 0.4415 0.4208 0.4271 0.3809

The results of Table 6 are presented graphically in FIG. 7. As can be seen, the correspondence of the vapor phase enthalpy compared to R-410A is very close over the entire temperature range.

The results for Table 6 for Example 15 compared to R-404A are shown in FIG. 8. As can be seen, the correspondence is good with the enthalpy for Example 15 being slightly higher.

Table 7 presents the liquid phase entropy versus temperature of R-410A and R-404A compared to Examples 1 to 8 and 15 of the disclosure.

TABLE 7 Liquid Phase Entropy Versus Temperature Relationship of Examples 1-8 and 15 of the Disclosure Compared to R-410A and R-404A. Ex. 1 Ex. 2 Ex. 3 Ex. 4 Ex. 5 Temp. Liquid Phase Liquid Phase Liquid Phase Liquid Phase Liquid Phase (° F.) Entropy (kJ/gR) Entropy (kJ/gR) Entropy (kJ/gR) Entropy (kJ/gR) Entropy (kJ/gR) −60 3.943 × 10⁻⁴ 3.952 × 10⁻⁴ 3.951 × 10⁻⁴ 3.953 × 10⁻⁴ 3.946 × 10⁻⁴ −55 4.037 × 10⁻⁴ 4.045 × 10⁻⁴ 4.044 × 10⁻⁴ 4.047 × 10⁻⁴ 4.040 × 10⁻⁴ −50 4.130 × 10⁻⁴ 4.138 × 10⁻⁴ 4.137 × 10⁻⁴ 4.139 × 10⁻⁴ 4.133 × 10⁻⁴ −45 4.222 × 10⁻⁴ 4.229 × 10⁻⁴ 4.229 × 10⁻⁴ 4.231 × 10⁻⁴ 4.225 × 10⁻⁴ −40 4.313 × 10⁻⁴ 4.320 × 10⁻⁴ 4.319 × 10⁻⁴ .4321 × 10⁻⁴ 4.316 × 10⁻⁴ −35 4.404 × 10⁻⁴ 4.410 × 10⁻⁴ 4.411 × 10⁻⁴ 4.411 × 10⁻⁴ 4.406 × 10⁻⁴ −30 4.493 × 10⁻⁴ 4.499 × 10⁻⁴ 4.499 × 10⁻⁴ 4.500 × 10⁻⁴ 4.496 × 10⁻⁴ −25 4.582 × 10⁻⁴ 4.588 × 10⁻⁴ 4.587 × 10⁻⁴ 4.589 × 10⁻⁴ 4.584 × 10⁻⁴ −20 4.671 × 10⁻⁴ 4.677 × 10⁻⁴ 4.675 × 10⁻⁴ 4.676 × 10⁻⁴ 4.673 × 10⁻⁴ −15 4.758 × 10⁻⁴ 4.763 × 10⁻⁴ 4.762 × 10⁻⁴ 4.763 × 10⁻⁴ 4.760 × 10⁻⁴ −10 4.845 × 10⁻⁴ 4.849 × 10⁻⁴ 4.849 × 10⁻⁴ 4.850 × 10⁻⁴ 4.847 × 10⁻⁴ −5 4.932 × 10⁻⁴ 4.935 × 10⁻⁴ 4.935 × 10⁻⁴ 4.936 × 10⁻⁴ 4.933 × 10⁻⁴ 0 5.018 × 10⁻⁴ 5.021 × 10⁻⁴ 5.020 × 10⁻⁴ 5.021 × 10⁻⁴ 5.019 × 10⁻⁴ 5 5.103 × 10⁻⁴ 5.106 × 10⁻⁴ 5.105 × 10⁻⁴ 5.105 × 10⁻⁴ 5.104 × 10⁻⁴ 10 5.188 × 10⁻⁴ 5.190 × 10⁻⁴ 5.190 × 10⁻⁴ 5.190 × 10⁻⁴ 5.188 × 10⁻⁴ 15 5.272 × 10⁻⁴ 5.274 × 10⁻⁴ 5.274 × 10⁻⁴ 5.274 × 10⁻⁴ 5.273 × 10⁻⁴ 20 5.356 × 10⁻⁴ 5.357 × 10⁻⁴ 5.357 × 10⁻⁴ 5.357 × 10⁻⁴ 5.356 × 10⁻⁴ 25 5.439 × 10⁻⁴ 5.440 × 10⁻⁴ 5.440 × 10⁻⁴ 5.440 × 10⁻⁴ 5.440 × 10⁻⁴ 30 5.522 × 10⁻⁴ 5.523 × 10⁻⁴ 5.523 × 10⁻⁴ 5.523 × 10⁻⁴ 5.523 × 10⁻⁴ 35 5.605 × 10⁻⁴ 5.605 × 10⁻⁴ 5.605 × 10⁻⁴ 5.605 × 10⁻⁴ 5.605 × 10⁻⁴ 40 5.688 × 10⁻⁴ 5.687 × 10⁻⁴ 5.687 × 10⁻⁴ 5.687 × 10⁻⁴ 5.687 × 10⁻⁴ 45 5.770 × 10⁻⁴ 5.768 × 10⁻⁴ 5.769 × 10⁻⁴ 5.768 × 10⁻⁴ 5.769 × 10⁻⁴ 50 5.852 × 10⁻⁴ 5.850 × 10⁻⁴ 5.850 × 10⁻⁴ 5.850 × 10⁻⁴ 5.851 × 10⁻⁴ 55 5.933 × 10⁻⁴ 5.931 × 10⁻⁴ 5.931 × 10⁻⁴ 5.931 × 10⁻⁴ 5.933 × 10⁻⁴ 60 6.015 × 10⁻⁴ 6.012 × 10⁻⁴ 6.012 × 10⁻⁴ 6.012 × 10⁻⁴ 6.014 × 10⁻⁴ 65 6.096 × 10⁻⁴ 6.093 × 10⁻⁴ 6.093 × 10⁻⁴ 6.093 × 10⁻⁴ 6.095 × 10⁻⁴ 70 6.177 × 10⁻⁴ 6.173 × 10⁻⁴ 6.174 × 10⁻⁴ 6.173 × 10⁻⁴ 6.176 × 10⁻⁴ 75 6.259 × 10⁻⁴ 6.254 × 10⁻⁴ 6.255 × 10⁻⁴ 6.254 × 10⁻⁴ 6.257 × 10⁻⁴ 80 6.340 × 10⁻⁴ 6.335 × 10⁻⁴ 6.335 × 10⁻⁴ 6.335 × 10⁻⁴ 6.338 × 10⁻⁴ 85 6.421 × 10⁻⁴ 6.415 × 10⁻⁴ 6.416 × 10⁻⁴ 6.415 × 10⁻⁴ 6.419 × 10⁻⁴ 90 6.502 × 10⁻⁴ 6.497 × 10⁻⁴ 6.497 × 10⁻⁴ 6.496 × 10⁻⁴ 6.501 × 10⁻⁴ 95 6.584 × 10⁻⁴ 6.577 × 10⁻⁴ 6.578 × 10⁻⁴ 6.577 × 10⁻⁴ 6.582 × 10⁻⁴ 100 6.666 × 10⁻⁴ 6.658 × 10⁻⁴ 6.659 × 10⁻⁴ 6.658 × 10⁻⁴ 6.664 × 10⁻⁴ 105 6.748 × 10⁻⁴ 6.740 × 10⁻⁴ 6.740 × 10⁻⁴ 6.740 × 10⁻⁴ 6.745 × 10⁻⁴ 110 6.830 × 10⁻⁴ 6.821 × 10⁻⁴ 6.822 × 10⁻⁴ 6.822 × 10⁻⁴ 6.828 × 10⁻⁴ 115 6.913 × 10⁻⁴ 6.903 × 10⁻⁴ 6.905 × 10⁻⁴ 6.904 × 10⁻⁴ 6.912 × 10⁻⁴ 120 6.997 × 10⁻⁴ 6.986 × 10⁻⁴ 6.987 × 10⁻⁴ 6.987 × 10⁻⁴ 6.994 × 10⁻⁴ 125 7.081 × 10⁻⁴ 7.070 × 10⁻⁴ 7.070 × 10⁻⁴ 7.071 × 10⁻⁴ 7.078 × 10⁻⁴ Ex. 6 Ex. 7 Ex. 8 R-410A Ex. 15 R-404A Temp. Liquid Phase Liquid Phase Liquid Phase Liquid Phase Liquid Phase Liquid Phase (° F.) Entropy (kJ/gR) Entropy (kJ/gR) Entropy (kJ/gR) Entropy (kJ/gR) Entropy (kJ/gR) Entropy (kJ/gR) −60 3.919 × 10⁻⁴ 3.943 × 10⁻⁴ 4.795 × 10⁻⁴ 3.922 × 10⁻⁴ 4.009 × 10⁻⁴ 4.064 × 10⁻⁴ −55 4.014 × 10⁻⁴ 4.037 × 10⁻⁴ 4.890 × 10⁻⁴ 4.017 × 10⁻⁴ 4.100 × 10⁻⁴ 4.150 × 10⁻⁴ −50 4.109 × 10⁻⁴ 4.130 × 10⁻⁴ 4.985 × 10⁻⁴ 4.111 × 10⁻⁴ 4.189 × 10⁻⁴ 4.235 × 10⁻⁴ −45 4.202 × 10⁻⁴ 4.222 × 10⁻⁴ 5.078 × 10⁻⁴ 4.204 × 10⁻⁴ 4.277 × 10⁻⁴ 4.320 × 10⁻⁴ −40 4.294 × 10⁻⁴ 4.313 × 10⁻⁴ 5.170 × 10⁻⁴ 4.296 × 10⁻⁴ 4.365 × 10⁻⁴ 4.403 × 10⁻⁴ −35 4.386 × 10⁻⁴ 4.404 × 10⁻⁴ 5.262 × 10⁻⁴ 4.387 × 10⁻⁴ 4.452 × 10⁻⁴ 4.487 × 10⁻⁴ −30 4.477 × 10⁻⁴ 4.494 × 10⁻⁴ 5.353 × 10⁻⁴ 4.478 × 10⁻⁴ 4.538 × 10⁻⁴ 4.569 × 10⁻⁴ −25 4.567 × 10⁻⁴ 4.583 × 10⁻⁴ 5.443 × 10⁻⁴ 4.568 × 10⁻⁴ 4.623 × 10⁻⁴ 4.651 × 10⁻⁴ −20 4.657 × 10⁻⁴ 4.671 × 10⁻⁴ 5.532 × 10⁻⁴ 4.657 × 10⁻⁴ 4.708 × 10⁻⁴ 4.733 × 10⁻⁴ −15 4.746 × 10⁻⁴ 4.759 × 10⁻⁴ 5.621 × 10⁻⁴ 4.745 × 10⁻⁴ 4.792 × 10⁻⁴ 4.814 × 10⁻⁴ −10 4.834 × 10⁻⁴ 4.846 × 10⁻⁴ 5.709 × 10⁻⁴ 4.833 × 10⁻⁴ 4.875 × 10⁻⁴ 4.894 × 10⁻⁴ −5 4.922 × 10⁻⁴ 4.932 × 10⁻⁴ 5.797 × 10⁻⁴ 4.921 × 10⁻⁴ 4.958 × 10⁻⁴ 4.974 × 10⁻⁴ 0 5.009 × 10⁻⁴ 5.018 × 10⁻⁴ 5.883 × 10⁻⁴ 5.008 × 10⁻⁴ 5.040 × 10⁻⁴ 5.054 × 10⁻⁴ 5 5.096 × 10⁻⁴ 5.103 × 10⁻⁴ 5.970 × 10⁻⁴ 5.095 × 10⁻⁴ 5.122 × 10⁻⁴ 5.133 × 10⁻⁴ 10 5.182 × 10⁻⁴ 5.188 × 10⁻⁴ 6.056 × 10⁻⁴ 5.181 × 10⁻⁴ 5.203 × 10⁻⁴ 5.212 × 10⁻⁴ 15 5.267 × 10⁻⁴ 5.272 × 10⁻⁴ 6.141 × 10⁻⁴ 5.266 × 10⁻⁴ 5.284 × 10⁻⁴ 5.291 × 10⁻⁴ 20 5.353 × 10⁻⁴ 5.356 × 10⁻⁴ 6.226 × 10⁻⁴ 5.352 × 10⁻⁴ 5.364 × 10⁻⁴ 5.369 × 10⁻⁴ 25 5.437 × 10⁻⁴ 5.439 × 10⁻⁴ 6.310 × 10⁻⁴ 5.437 × 10⁻⁴ 5.444 × 10⁻⁴ 5.447 × 10⁻⁴ 30 5.522 × 10⁻⁴ 5.522 × 10⁻⁴ 6.394 × 10⁻⁴ 5.522 × 10⁻⁴ 5.524 × 10⁻⁴ 5.525 × 10⁻⁴ 35 5.606 × 10⁻⁴ 5.605 × 10⁻⁴ 6.478 × 10⁻⁴ 5.606 × 10⁻⁴ 5.603 × 10⁻⁴ 5.602 × 10⁻⁴ 40 5.690 × 10⁻⁴ 5.688 × 10⁻⁴ 6.561 × 10⁻⁴ 5.691 × 10⁻⁴ 5.682 × 10⁻⁴ 5.679 × 10⁻⁴ 45 5.773 × 10⁻⁴ 5.770 × 10⁻⁴ 6.644 × 10⁻⁴ 5.775 × 10⁻⁴ 5.760 × 10⁻⁴ 5.757 × 10⁻⁴ 50 5.857 × 10⁻⁴ 5.851 × 10⁻⁴ 6.727 × 10⁻⁴ 5.859 × 10⁻⁴ 5.839 × 10⁻⁴ 5.834 × 10⁻⁴ 55 5.940 × 10⁻⁴ 5.933 × 10⁻⁴ 6.809 × 10⁻⁴ 5.944 × 10⁻⁴ 5.917 × 10⁻⁴ 5.911 × 10⁻⁴ 60 6.023 × 10⁻⁴ 6.014 × 10⁻⁴ 6.892 × 10⁻⁴ 6.028 × 10⁻⁴ 5.995 × 10⁻⁴ 5.988 × 10⁻⁴ 65 6.106 × 10⁻⁴ 6.096 × 10⁻⁴ 6.974 × 10⁻⁴ 6.112 × 10⁻⁴ 6.072 × 10⁻⁴ 6.065 × 10⁻⁴ 70 6.189 × 10⁻⁴ 6.177 × 10⁻⁴ 7.056 × 10⁻⁴ 6.197 × 10⁻⁴ 6.150 × 10⁻⁴ 6.142 × 10⁻⁴ 75 6.271 × 10⁻⁴ 6.258 × 10⁻⁴ 7.138 × 10⁻⁴ 6.281 × 10⁻⁴ 6.227 × 10⁻⁴ 6.219 × 10⁻⁴ 80 6.354 × 10⁻⁴ 6.339 × 10⁻⁴  7220 × 10⁻⁴ 6.367 × 10⁻⁴ 6.304 × 10⁻⁴ 6.297 × 10⁻⁴ 85 6.437 × 10⁻⁴ 6.420 × 10⁻⁴ 7.302 × 10⁻⁴ 6.453 × 10⁻⁴ 6.382 × 10⁻⁴ 6.374 × 10⁻⁴ 90 6.520 × 10⁻⁴ 6.501 × 10⁻⁴ 7.384 × 10⁻⁴ 6.539 × 10⁻⁴ 6.459 × 10⁻⁴ 6.452 × 10⁻⁴ 95 6.603 × 10⁻⁴ 6.582 × 10⁻⁴ 7.466 × 10⁻⁴ 6.625 × 10⁻⁴ 6.536 × 10⁻⁴  6531 × 10⁻⁴ 100 6.687 × 10⁻⁴ 6.664 × 10⁻⁴ 7.548 × 10⁻⁴ 6.713 × 10⁻⁴ 6.614 × 10⁻⁴ 6.610 × 10⁻⁴ 105 6.770 × 10⁻⁴ 6.746 × 10⁻⁴ 7.631 × 10⁻⁴ 6.801 × 10⁻⁴ 6.691 × 10⁻⁴ 6.690 × 10⁻⁴ 110 6.855 × 10⁻⁴ 6.828 × 10⁻⁴ 7.714 × 10⁻⁴ 6.890 × 10⁻⁴ 6.769 × 10⁻⁴ 6.770 × 10⁻⁴ 115 6.939 × 10⁻⁴ 6.910 × 10⁻⁴ 7.797 × 10⁻⁴ 6.981 × 10⁻⁴ 6.847 × 10⁻⁴ 6.852 × 10⁻⁴ 120 7.025 × 10⁻⁴ 6.994 × 10⁻⁴ 7.881 × 10⁻⁴ 7.074 × 10⁻⁴ 6.926 × 10⁻⁴ 6.935 × 10⁻⁴ 125 7.111 × 10⁻⁴ 7.078 × 10⁻⁴ 7.966 × 10⁻⁴ 7.169 × 10⁻⁴ 7.005 × 10⁻⁴ 7.019 × 10⁻⁴

The results of Table 7 are presented graphically in FIG. 9. As can be seen, the correspondence of the liquid phase entropy pressure to R-410A is very close over the entire temperature range.

The results for Example 15 compared to R-404A are presented graphically in FIG. 10. As can be seen, the correspondence is so close that the curves overlap.

Table 8 presents the vapor phase entropy versus temperature of R-410A and R-404A compared to Examples 1 to 8 and 15 of the disclosure.

TABLE 8 Vapor Phase Entropy Versus Temperature Relationship of Examples 1-8 and 15 of the Disclosure Compared to R-410A and R-404A. Ex. 1 Ex. 2 Ex. 3 Ex. 4 Ex. 5 Temp. Vapor Phase Vapor Phase Vapor Phase Vapor Phase Vapor Phase (° F.) Entropy (kJ/gR) Entropy (kJ/gR) Entropy (kJ/gR) Entropy (kJ/gR) Entropy (kJ/gR) −60 1.073 × 10⁻³ 1.066 × 10⁻³ 1.067 × 10⁻³ 1.064 × 10⁻³ 1.071 × 10⁻³ −55 1.069 × 10⁻³ 1.062 × 10⁻³ 1.062 × 10⁻³ 1.059 × 10⁻³ 1.066 × 10⁻³ −50 1.064 × 10⁻³ 1.057 × 10⁻³ 1.058 × 10⁻³ 1.055 × 10⁻³ 1.062 × 10⁻³ −45 1.060 × 10⁻³ 1.053 × 10⁻³ 1.054 × 10⁻³ 1.051 × 10⁻³ 1.058 × 10⁻³ −40 1.056 × 10⁻³ 1.049 × 10⁻³ 1.050 × 10⁻³ 1.047 × 10⁻³ 1.054 × 10⁻³ −35 1.052 × 10⁻³ 1.046 × 10⁻³ 1.047 × 10⁻³ 1.044 × 10⁻³ 1.050 × 10⁻³ −30 1.049 × 10⁻³ 1.042 × 10⁻³ 1.043 × 10⁻³ 1.040 × 10⁻³ 1.047 × 10⁻³ −25 1.045 × 10⁻³ 1.039 × 10⁻³ 1.040 × 10⁻³ 1.037 × 10⁻³ 1.043 × 10⁻³ −20 1.042 × 10⁻³ 1.036 × 10⁻³ 1.037 × 10⁻³ 1.038 × 10⁻³ 1.040 × 10⁻³ −15 1.039 × 10⁻³ 1.033 × 10⁻³ 1.033 × 10⁻³ 1.031 × 10⁻³ 1.037 × 10⁻³ −10 1.036 × 10⁻³ 1.030 × 10⁻³ 1.031 × 10⁻³ 1.028 × 10⁻³ 1.034 × 10⁻³ −5 1.033 × 10⁻³ 1.027 × 10⁻³ 1.028 × 10⁻³ 1.025 × 10⁻³ 1.031 × 10⁻³ 0 1.030 × 10⁻³ 1.024 × 10⁻³ 1.025 × 10⁻³ 1.022 × 10⁻³ 1.028 × 10⁻³ 5 1.027 × 10⁻³ 1.022 × 10⁻³ 1.022 × 10⁻³ 1.020 × 10⁻³ 1.025 × 10⁻³ 10 1.025 × 10⁻³ 1.019 × 10⁻³ 1.020 × 10⁻³ 1.017 × 10⁻³ 1.023 × 10⁻³ 15 1.022 × 10⁻³ 1.017 × 10⁻³ 1.018 × 10⁻³ 1.015 × 10⁻³ 1.020 × 10⁻³ 20 1.020 × 10⁻³ 1.015 × 10⁻³ 1.015 × 10⁻³ 1.013 × 10⁻³ 1.018 × 10⁻³ 25 1.018 × 10⁻³ 1.012 × 10⁻³ 1.013 × 10⁻³ 1.010 × 10⁻³ 1.016 × 10⁻³ 30 1.015 × 10⁻³ 1.010 × 10⁻³ 1.011 × 10⁻³ 1.008 × 10⁻³ 1.013 × 10⁻³ 35 1.013 × 10⁻³ 1.008 × 10⁻³ 1.009 × 10⁻³ 1.006 × 10⁻³ 1.011 × 10⁻³ 40 1.011 × 10⁻³ 1.006 × 10⁻³ 1.007 × 10⁻³ 1.004 × 10⁻³ 1.009 × 10⁻³ 45 1.009 × 10⁻³ 1.004 × 10⁻³ 1.005 × 10⁻³ 1.002 × 10⁻³ 1.007 × 10⁻³ 50 1.007 × 10⁻³ 1.002 × 10⁻³ 1.003 × 10⁻³ 1.000 × 10⁻³ 1.005 × 10⁻³ 55 1.005 × 10⁻³ 1.000 × 10⁻³ 1.001 × 10⁻³ 9.981 × 10⁻⁴ 1.003 × 10⁻³ 60 1.003 × 10⁻³ 9.983 × 10⁻⁴ 9.988 × 10⁻⁴ 9.962 × 10⁻⁴ 1.001 × 10⁻³ 65 1.001 × 10⁻³ 9.965 × 10⁻⁴ 9.969 × 10⁻⁴ 9.943 × 10⁻⁴ 9.989 × 10⁻⁴ 70 9.988 × 10⁻⁴ 9.947 × 10⁻⁴ 9.951 × 10⁻⁴ 9.925 × 10⁻⁴ 9.970 × 10⁻⁴ 75 9.969 × 10⁻⁴ 9.929 × 10⁻⁴ 9.932 × 10⁻⁴ 9.907 × 10⁻⁴ 9.951 × 10⁻⁴ 80 9.949 × 10⁻⁴ 9.910 × 10⁻⁴ 9.914 × 10⁻⁴ 9.888 × 10⁻⁴ 9.932 × 10⁻⁴ 85 9.930 × 10⁻⁴ 9.892 × 10⁻⁴ 9.895 × 10⁻⁴ 9.870 × 10⁻⁴ 9.912 × 10⁻⁴ 90 9.910 × 10⁻⁴ 9.874 × 10⁻⁴ 9.877 × 10⁻⁴ 9.851 × 10⁻⁴ 9.893 × 10⁻⁴ 95 9.891 × 10⁻⁴ 9.855 × 10⁻⁴ 9.858 × 10⁻⁴ 9.832 × 10⁻⁴ 9.873 × 10⁻⁴ 100 9.870 × 10⁻⁴ 9.836 × 10⁻⁴ 9.839 × 10⁻⁴ 9.813 × 10⁻⁴ 9.853 × 10⁻⁴ 105 9.850 × 10⁻⁴ 9.817 × 10⁻⁴ 9.819 × 10⁻⁴ 9.794 × 10⁻⁴ 9.832 × 10⁻⁴ 110 9.829 × 10⁻⁴ 9.797 × 10⁻⁴ 9.799 × 10⁻⁴ 9.773 × 10⁻⁴ 9.811 × 10⁻⁴ 115 9.806 × 10⁻⁴ 9.777 × 10⁻⁴ 9.778 × 10⁻⁴ 9.752 × 10⁻⁴ 9.789 × 10⁻⁴ 120 9.784 × 10⁻⁴ 9.755 × 10⁻⁴ 9.757 × 10⁻⁴ 9.731 × 10⁻⁴ 9.767 × 10⁻⁴ 125 9.760 × 10⁻⁴ 9.733 × 10⁻⁴ 9.734 × 10⁻⁴ 9.708 × 10⁻⁴ 9.743 × 10⁻⁴ Ex. 6 Ex. 7 Ex. 8 R-410A Ex. 15 R-404A Temp. Vapor Phase Vapor Phase Vapor Phase Vapor Phase Vapor Phase Vapor Phase (° F.) Entropy (kJ/gR) Entropy (kJ/gR) Entropy (kJ/gR) Entropy (kJ/gR) Entropy (kJ/gR) Entropy (kJ/gR) −60 1.068 × 10⁻³ 1.072 × 10⁻³ 1.173 × 10⁻³ 1.075 × 10⁻³ 1.028 × 10⁻³ 9.171 × 10⁻³ −55 1.063 × 10⁻³ 1.068 × 10⁻³ 1.168 × 10⁻³ 1.070 × 10⁻³ 1.024 × 10⁻³ 9.149 × 10⁻³ −50 1.059 × 10⁻³ 1.063 × 10⁻³ 1.164 × 10⁻³ 1.065 × 10⁻³ 1.021 × 10⁻³ 9.129 × 10⁻³ −45 1.055 × 10⁻³ 1.059 × 10⁻³ 1.160 × 10⁻³ 1.060 × 10⁻³ 1.017 × 10⁻³ 9.110 × 10⁻³ −40 1.051 × 10⁻³ 1.055 × 10⁻³ 1.155 × 10⁻³ 1.056 × 10⁻³ 1.014 × 10⁻³ 9.092 × 10⁻³ −35 1.047 × 10⁻³ 1.052 × 10⁻³ 1.152 × 10⁻³ 1.052 × 10⁻³ 1.011 × 10⁻³ 9.075 × 10⁻³ −30 1.044 × 10⁻³ 1.048 × 10⁻³ 1.148 × 10⁻³ 1.048 × 10⁻³ 1.008 × 10⁻³ 9.060 × 10⁻⁴ −25 1.040 × 10⁻³ 1.045 × 10⁻³ 1.144 × 10⁻³ 1.044 × 10⁻³ 1.006 × 10⁻³ 9.046 × 10⁻⁴ −20 1.037 × 10⁻³ 1.041 × 10⁻³ 1.141 × 10⁻³ 1.040 × 10⁻³ 1.003 × 10⁻³ 9.032 × 10⁻⁴ −15 1.034 × 10⁻³ 1.038 × 10⁻³ 1.138 × 10⁻³ 1.036 × 10⁻³ 1.001 × 10⁻³ 9.020 × 10⁻⁴ −10 1.031 × 10⁻³ 1.035 × 10⁻³ 1.135 × 10⁻³ 1.033 × 10⁻³ 9.983 × 10⁻⁴ 9.008 × 10⁻⁴ −5 1.029 × 10⁻³ 1.032 × 10⁻³ 1.132 × 10⁻³ 1.029 × 10⁻³ 9.961 × 10⁻⁴ 8.997 × 10⁻⁴ 0 1.026 × 10⁻³ 1.030 × 10⁻³ 1.129 × 10⁻³ 1.026 × 10⁻³ 9.940 × 10⁻⁴ 8.986 × 10⁻⁴ 5 1.023 × 10⁻³ 1.027 × 10⁻³ 1.126 × 10⁻³ 1.023 × 10⁻³ 9.920 × 10⁻⁴ 8.977 × 10⁻⁴ 10 1.021 × 10⁻³ 1.025 × 10⁻³ 1.124 × 10⁻³ 1.019 × 10⁻³ 9.901 × 10⁻⁴ 8.967 × 10⁻⁴ 15 1.018 × 10⁻³ 1.022 × 10⁻³ 1.121 × 10⁻³ 1.016 × 10⁻³ 9.883 × 10⁻⁴ 8.959 × 10⁻⁴ 20 1.016 × 10⁻³ 1.020 × 10⁻³ 1.119 × 10⁻³ 1.013 × 10⁻³ 9.866 × 10⁻⁴ 8.951 × 10⁻⁴ 25 1.014 × 10⁻³ 1.018 × 10⁻³ 1.116 × 10⁻³ 1.010 × 10⁻³ 9.849 × 10⁻⁴ 8.943 × 10⁻⁴ 30 1.012 × 10⁻³ 1.015 × 10⁻³ 1.114 × 10⁻³ 1.007 × 10⁻³ 9.833 × 10⁻⁴ 8.935 × 10⁻⁴ 35 1.010 × 10⁻³ 1.013 × 10⁻³ 1.112 × 10⁻³ 1.004 × 10⁻³ 9.818 × 10⁻⁴ 8.928 × 10⁻⁴ 40 1.008 × 10⁻³ 1.011 × 10⁻³ 1.109 × 10⁻³ 1.001 × 10⁻³ 9.803 × 10⁻⁴ 8.921 × 10⁻⁴ 45 1.006 × 10⁻³ 1.009 × 10⁻³ 1.107 × 10⁻³ 9.981 × 10⁻⁴ 9.789 × 10⁻⁴ 8.914 × 10⁻⁴ 50 1.004 × 10⁻³ 1.007 × 10⁻³ 1.105 × 10⁻³ 9.951 × 10⁻⁴ 9.775 × 10⁻⁴ 8.907 × 10⁻⁴ 55 1.002 × 10⁻³ 1.005 × 10⁻³ 1.103 × 10⁻³ 9.922 × 10⁻⁴ 9.762 × 10⁻⁴ 8.899 × 10⁻⁴ 60 1.000 × 10⁻³ 1.003 × 10⁻³ 1.101 × 10⁻³ 9.892 × 10⁻⁴ 9.749 × 10⁻⁴ 8.892 × 10⁻⁴ 65 9.981 × 10⁻⁴ 1.001 × 10⁻³ 1.099 × 10⁻³ 9.862 × 10⁻⁴ 9.736 × 10⁻⁴ 8.885 × 10⁻⁴ 70 9.963 × 10⁻⁴ 9.994 × 10⁻⁴ 1.097 × 10⁻³ 9.832 × 10⁻⁴ 9.723 × 10⁻⁴ 8.877 × 10⁻⁴ 75 9.945 × 10⁻⁴ 9.975 × 10⁻⁴ 1.095 × 10⁻³ 9.801 × 10⁻⁴ 9.711 × 10⁻⁴ 8.869 × 10⁻⁴ 80 9.927 × 10⁻⁴ 9.957 × 10⁻⁴ 1.094 × 10⁻³ 9.770 × 10⁻⁴ 9.698 × 10⁻⁴ 8.861 × 10⁻⁴ 85 9.991 × 10⁻⁴ 9.938 × 10⁻⁴ 1.092 × 10⁻³ 9.737 × 10⁻⁴ 9.686 × 10⁻⁴ 8.851 × 10⁻⁴ 90 9.890 × 10⁻⁴ 9.919 × 10⁻⁴ 1.090 × 10⁻³ 9.704 × 10⁻⁴ 9.673 × 10⁻⁴ 8.842 × 10⁻⁴ 95 9.871 × 10⁻⁴ 9.900 × 10⁻⁴ 1.088 × 10⁻³ 9.669 × 10⁻⁴ 9.660 × 10⁻⁴ 8.831 × 10⁻⁴ 100 9.852 × 10⁻⁴ 9.881 × 10⁻⁴ 1.086 × 10⁻³ 9.633 × 10⁻⁴ 9.648 × 10⁻⁴ 8.819 × 10⁻⁴ 105 9.833 × 10⁻⁴ 9.861 × 10⁻⁴ 1.084 × 10⁻³ 9.596 × 10⁻⁴ 9.634 × 10⁻⁴ 8.806 × 10⁻⁴ 110 9.812 × 10⁻⁴ 9.841 × 10⁻⁴ 1.082 × 10⁻³ 9.556 × 10⁻⁴ 9.621 × 10⁻⁴ 8.791 × 10⁻⁴ 115 9.791 × 10⁻⁴ 9.820 × 10⁻⁴ 1.080 × 10⁻³ 9.513 × 10⁻⁴ 9.607 × 10⁻⁴ 8.775 × 10⁻⁴ 120 9.769 × 10⁻⁴ 9.800 × 10⁻⁴ 1.077 × 10⁻³ 9.468 × 10⁻⁴ 9.592 × 10⁻⁴ 8.756 × 10⁻⁴ 125 9.746 × 10⁻⁴ 9.775 × 10⁻⁴ 1.075 × 10⁻³ 9.418 × 10⁻⁴ 9.577 × 10⁻⁴ 8.735 × 10⁻⁴

The results of Table 8 are presented graphically in FIG. 11. As can be seen, the correspondence of the vapor phase entropy pressure to R-410A is very close over the entire temperature range.

The results of Table 8 for Example 15 and R-404A are presented graphically in FIG. 12. As can be seen, the correspondence is good with the vapor phase entropy for Example 15 being slightly higher.

The NIST REFPROP program was used to generate the thermodynamic values for the examples of the disclosure. The results for temperature, pressure, density, enthalpy and entropy for Examples 1-8 are set forth in Tables 9-16.

TABLE 9 Temperature, Pressure, Density, Enthalpy and Entropy Values for Example 1. Liquid Vapor Liquid Vapor Phase Phase Phase Phase Temp. Pressure Pressure Density Density (° F.) (psia) (psia) (g/cm³) (g/cm³) −60 20.57 7.057 1.347 2.132 × 10⁻³ −55 23.25 8.257 1.339 2.470 × 10⁻³ −50 26.19 9.617 1.331 2.850 × 10⁻³ −45 29.40 11.15 1.322 3.274 × 10⁻³ −40 32.92 12.87 1.314 3.746 × 10⁻³ −35 36.74 14.80 1.305 4.271 × 10⁻³ −30 40.89 16.95 1.297 4.850 × 10⁻³ −25 45.39 19.35 1.288 5.494 × 10⁻³ −20 50.26 22.00 1.279 6.201 × 10⁻³ −15 55.50 24.93 1.270 6.978 × 10⁻³ −10 61.16 28.15 1.262 7.830 × 10⁻³ −5 67.23 31.70 1.252 8.762 × 10⁻³ 0 73.74 35.58 1.243 9.779 × 10⁻³ 5 80.70 39.83 1.234 0.01089 10 88.15 44.46 1.225 0.01209 15 96.09 49.50 1.215 0.01340 20 104.5 55.00 1.206 0.01482 25 113.5 60.89 1.196 0.01636 30 123.1 67.30 1.186 0.01802 35 133.2 74.21 1.176 0.01980 40 143.9 81.65 1.167 0.02176 45 155.2 89.66 1.155 0.02385 50 167.2 98.26 1.145 0.02611 55 179.8 107.5 1.134 0.02853 60 193.1 117.3 1.123 0.03115 65 207.0 127.9 1.112 0.03400 70 221.7 139.1 1.100 0.03699 75 237.1 151.1 1.088 0.04024 80 253.2 163.9 1.076 0.04375 85 270.1 177.5 1.064 0.04752 90 287.8 192.0 1.051 0.05157 95 306.3 207.3 1.038 0.05595 100 325.6 223.6 1.025 0.06066 105 345.8 240.8 1.011 0.06574 110 366.8 259.1 0.9967 0.07124 115 388.2 278.4 0.9818 0.07719 120 411.4 298.9 0.9664 0.08363 Liquid Vapor Liquid Vapor Phase Phase Phase Phase Temp. Enthalpy Enthalpy Entropy Entropy (° F.) (kJ/g) (kJ/g) (kJ/gR) (kJ/gR) −60 0.1277 0.3883 3.940 × 10⁻⁴ 1.073 × 10⁻³ −55 0.1315 0.3901 4.037 × 10⁻⁴ 1.069 × 10⁻³ −50 0.1353 0.3918 4.130 × 10⁻⁴ 1.064 × 10⁻³ −45 0.1391 0.3936 4.222 × 10⁻⁴ 1.060 × 10⁻³ −40 0.1429 0.3953 4.313 × 10⁻⁴ 1.056 × 10⁻³ −35 0.1468 0.3970 4.404 × 10⁻⁴ 1.052 × 10⁻³ −30 0.1506 0.3988 4.493 × 10⁻⁴ 1.049 × 10⁻³ −25 0.1545 0.4004 4.582 × 10⁻⁴ 1.045 × 10⁻³ −20 0.1584 0.4021 4.671 × 10⁻⁴ 1.042 × 10⁻³ −15 0.1623 0.4038 4.758 × 10⁻⁴ 1.039 × 10⁻³ −10 0.1662 0.4054 4.845 × 10⁻⁴ 1.036 × 10⁻³ −5 0.1702 0.4071 4.932 × 10⁻⁴ 1.033 × 10⁻³ 0 0.1741 0.4087 5.018 × 10⁻⁴ 1.030 × 10⁻³ 5 0.1781 0.4103 5.103 × 10⁻⁴ 1.027 × 10⁻³ 10 0.1821 0.4118 5.188 × 10⁻⁴ 1.025 × 10⁻³ 15 0.1861 0.4134 5.272 × 10⁻⁴ 1.022 × 10⁻³ 20 0.1902 0.4149 5.356 × 10⁻⁴ 1.020 × 10⁻³ 25 0.1943 0.4164 5.439 × 10⁻⁴ 1.019 × 10⁻³ 30 0.1984 0.4179 5.522 × 10⁻⁴ 1.015 × 10⁻³ 35 0.2025 0.4193 5.605 × 10⁻⁴ 1.013 × 10⁻³ 40 0.2066 0.4207 5.688 × 10⁻⁴ 1.011 × 10⁻³ 45 0.2108 0.4221 5.770 × 10⁻⁴ 1.009 × 10⁻³ 50 0.2151 0.4234 5.852 × 10⁻⁴ 1.007 × 10⁻³ 55 0.2193 0.4247 5.933 × 10⁻⁴ 1.005 × 10⁻³ 60 0.2236 0.4259 6.015 × 10⁻⁴ 1.003 × 10⁻³ 65 0.2279 0.4271 6.100 × 10⁻⁴ 1.001 × 10⁻³ 70 0.2323 0.4283 6.177 × 10⁻⁴ 9.988 × 10⁻⁴ 75 0.2367 0.4294 6.259 × 10⁻⁴ 9.969 × 10⁻⁴ 80 0.2412 0.4305 6.340 × 10⁻⁴ 9.949 × 10⁻⁴ 85 0.2457 0.4315 6.421 × 10⁻⁴ 9.930 × 10⁻⁴ 90 0.2503 0.4324 6.502 × 10⁻⁴ 9.910 × 10⁻⁴ 95 0.2549 0.4333 6.583 × 10⁻⁴ 9.890 × 10⁻⁴ 100 0.2596 0.4341 6.666 × 10⁻⁴ 9.870 × 10⁻⁴ 105 0.2643 0.4348 6.748 × 10⁻⁴ 9.850 × 10⁻⁴ 110 0.2692 0.4354 6.830 × 10⁻⁴ 9.828 × 10⁻⁴ 115 0.2741 0.4360 6.913 × 10⁻⁴ 9.806 × 10⁻⁴ 120 0.2790 0.4364 6.997 × 10⁻⁴ 9.784 × 10⁻⁴

TABLE 10 Temperature, Pressure, Density, Enthalpy and Entropy Values for Example 2. Liquid Vapor Liquid Vapor Phase Phase Phase Phase Temp. Pressure Pressure Density Density (° F.) (psia) (psia) (g/cm³) (g/cm³) −60 20.44 6.787 1.351 2.084 × 10⁻³ −55 23.09 7.946 1.343 2.415 × 10⁻³ −50 26.00 9.258 1.335 2.787 × 10⁻³ −45 29.19 10.74 1.326 3.203 × 10⁻³ −40 32.67 12.41 1.318 3.667 × 10⁻³ −35 36.45 14.27 1.340 4.183 × 10⁻³ −30 40.56 16.35 1.301 4.754 × 10⁻³ −25 45.01 18.67 1.292 5.385 × 10⁻³ −20 49.83 21.24 1.284 6.080 × 10⁻³ −15 55.02 24.08 1.275 6.844 × 10⁻³ −10 60.60 27.20 1.266 7.682 × 10⁻³ −5 66.60 30.64 1.257 8.599 × 10⁻³ 0 73.03 34.41 1.248 9.600 × 10⁻³ 5 79.91 38.54 1.238 0.01069 10 87.27 43.03 1.229 0.01188 15 95.11 47.93 1.220 0.01317 20 103.5 53.24 1.210 0.01457 25 112.3 59.00 1.200 0.01608 30 121.7 65.22 1.190 0.01772 35 131.7 71.95 1.180 0.01949 40 142.3 79.19 1.170 0.02140 45 153.5 86.98 1.160 0.02346 50 165.2 95.35 1.149 0.02568 55 177.7 104.3 1.139 0.02808 60 190.7 113.9 1.129 0.03065 65 204.5 124.2 1.116 0.03342 70 218.9 135.2 1.105 0.03640 75 234.1 146.9 1.093 0.03960 80 250.0 159.3 1.081 0.04306 85 266.6 172.6 1.069 0.04680 90 284.0 186.7 1.056 0.05076 95 302.2 201.6 1.044 0.05507 100 321.2 217.5 1.030 0.05970 105 341.0 234.3 1.016 0.06470 110 361.7 252.2 1.002 0.07010 115 383.1 271.0 0.9874 0.07594 120 405.5 291.0 0.9720 0.08226 125 428.7 312.1 0.9561 0.08913 Liquid Vapor Liquid Vapor Phase Phase Phase Phase Temp. Enthalpy Enthalpy Entropy Entropy (° F.) (kJ/g) (kJ/g) (kJ/gR) (kJ/gR) −60 0.1281 0.3854 3.952 × 10⁻⁴ 1.066 × 10⁻³ −55 0.1319 0.3872 4.045 × 10⁻⁴ 1.062 × 10⁻³ −50 0.1357 0.3889 4.138 × 10⁻⁴ 1.057 × 10⁻³ −45 0.1395 0.3907 4.229 × 10⁻⁴ 1.053 × 10⁻³ −40 0.1433 0.3925 4.320 × 10⁻⁴ 1.049 × 10⁻³ −35 0.1471 0.3942 4.410 × 10⁻⁴ 1.046 × 10⁻³ −30 0.1509 0.3959 4.499 × 10⁻⁴ 1.042 × 10⁻³ −25 0.1548 0.3976 4.588 × 10⁻⁴ 1.039 × 10⁻³ −20 0.1586 0.3993 4.676 × 10⁻⁴ 1.039 × 10⁻³ −15 0.1625 0.4010 4.730 × 10⁻⁴ 1.033 × 10⁻³ −10 0.1664 0.4027 4.849 × 10⁻⁴ 1.030 × 10⁻³ −5 0.1703 0.4043 4.935 × 10⁻⁴ 1.027 × 10⁻³ 0 0.1743 0.4060 5.021 × 10⁻⁴ 1.024 × 10⁻³ 5 0.1782 0.4076 5.106 × 10⁻⁴ 1.022 × 10⁻³ 10 0.1822 0.4092 5.190 × 10⁻⁴ 1.019 × 10⁻³ 15 0.1862 0.4107 5.274 × 10⁻⁴ 1.017 × 10⁻³ 20 0.1902 0.4123 5.357 × 10⁻⁴ 1.015 × 10⁻³ 25 0.1943 0.4138 5.440 × 10⁻⁴ 1.012 × 10⁻³ 30 0.1984 0.4153 5.523 × 10⁻⁴ 1.010 × 10⁻³ 35 0.2024 0.4168 5.605 × 10⁻⁴ 1.008 × 10⁻³ 40 0.2070 0.4181 5.687 × 10⁻⁴ 1.050 × 10⁻³ 45 0.2108 0.4196 5.769 × 10⁻⁴ 1.004 × 10⁻³ 50 0.2150 0.4210 5.850 × 10⁻⁴ 1.002 × 10⁻³ 55 0.2192 0.4223 5.931 × 10⁻⁴ 1.000 × 10⁻³ 60 0.2235 0.4236 6.012 × 10⁻⁴ 9.983 × 10⁻⁴ 65 0.2278 0.4248 6.093 × 10⁻⁴ 9.965 × 10⁻⁴ 70 0.2321 0.4260 6.173 × 10⁻⁴ 9.947 × 10⁻⁴ 75 0.2377 0.4272 6.254 × 10⁻⁴ 9.929 × 10⁻⁴ 80 0.2409 0.4283 6.335 × 10⁻⁴ 9.910 × 10⁻⁴ 85 0.2454 0.4293 6.415 × 10⁻⁴ 9.892 × 10⁻⁴ 90 0.2499 0.4303 6.496 × 10⁻⁴ 9.874 × 10⁻⁴ 95 0.2545 0.4312 6.577 × 10⁻⁴ 9.855 × 10⁻⁴ 100 0.2592 0.4321 6.658 × 10⁻⁴ 9.836 × 10⁻⁴ 105 0.2639 0.4329 6.740 × 10⁻⁴ 9.820 × 10⁻⁴ 110 0.2687 0.4336 .6821 × 10⁻⁴ 9.800 × 10⁻⁴ 115 0.2735 0.4342 6.903 × 10⁻⁴ 9.777 × 10⁻⁴ 120 0.2784 0.4347 6.986 × 10⁻⁴ 9.755 × 10⁻⁴ 125 0.2835 0.4351 7.070 × 10⁻⁴ 9.732 × 10⁻⁴

TABLE 11 Temperature, Pressure, Density, Enthalpy and Entropy Values for Example 3. Liquid Vapor Liquid Phase Phase Phase Vapor Phase Temp. Pressure Pressure Density Density (° F.) (psia) (psia) (g/cm³) (g/cm³) −60 20.47 6.840 1.352 2.097 × 10⁻³ −55 23.12 8.006 1.344 2.430 × 10⁻³ −50 26.04 9.328 1.336 2.804 × 10⁻³ −45 29.23 10.82 1.327 3.222 × 10⁻³ −40 32.71 12.50 1.319 3.689 × 10⁻³ −35 36.49 14.37 1.310 4.207 × 10⁻³ −30 40.61 16.47 1.302 4.780 × 10⁻³ −25 45.06 18.80 1.293 5.414 × 10⁻³ −20 49.88 21.38 1.284 6.113 × 10⁻³ −15 55.07 24.23 1.275 6.881 × 10⁻³ −10 60.66 27.38 1.266 7.722 × 10⁻³ −5 66.66 30.84 1.257 8.643 × 10⁻³ 0 73.10 34.63 1.248 9.649 × 10⁻³ 5 79.98 38.77 1.239 0.01075 10 87.34 43.29 1.230 0.01194 15 95.19 48.21 1.220 0.01323 20 103.5 53.56 1.211 0.01464 25 112.4 59.34 1.201 0.01616 30 121.8 65.60 1.191 0.01780 35 131.8 72.36 1.181 0.01958 40 142. 79.64 1.171 0.02150 45 153.6 87.47 1.160 0.02357 50 165.4 95.87 1.150 0.02580 55 177.8 104.9 1.139 0.02821 60 190.9 114.5 1.128 0.03079 65 204.7 124.9 1.117 0.03358 70 219.1 135.9 1.105 0.03657 75 234.3 147.6 1.094 0.03979 80 250.2 160.1 1.082 0.04326 85 266.9 173.5 1.069 0.04699 90 284.3 187.6 1.057 0.05100 95 302.5 202.6 1.044 0.05532 100 321.6 218.6 1.030 0.05998 105 341.4 235.6 1.017 0.06501 110 362.1 253.4 1.002 0.07044 115 383.6 272.3 0.9876 0.07631 120 406.0 292.4 0.9722 0.08267 125 429.2 313.6 0.9562 0.08959 Liquid Vapor Liquid Vapor Phase Phase Phase Phase Temp. Enthalpy Enthalpy Entropy Entropy (° F.) (kJ/g) (kJ/g) (kJ/gR) (kJ/gR) −60 0.1281 0.3859 0.0003951 1.067 × 10⁻³ −55 0.1318 0.3876 0.0004044 1.062 × 10⁻³ −50 0.1356 0.3890 0.0004137 1.058 × 10⁻³ −45 0.1394 0.3912 4.229 × 10⁻⁴ 1.054 × 10⁻³ −40 0.1432 0.3929 4.319 × 10⁻⁴ 1.050 × 10⁻³ −35 0.1471 0.3946 4.410 × 10⁻⁴ 1.047 × 10⁻³ −30 0.1509 0.3964 4.508 × 10⁻⁴ 1.043 × 10⁻³ −25 0.1547 0.3981 4.587 × 10⁻⁴ 1.040 × 10⁻³ −20 0.1586 0.3998 0.0004.675 1.037 × 10⁻³ −15 0.1625 0.4014  4762 × 10⁻⁴ 1.033 × 10⁻³ −10 0.1664 0.4031 4.849 × 10⁻⁴ 1.031 × 10⁻³ −5 0.1703 0.4047 4.935 × 10⁻⁴ 1.028 × 10⁻³ 0 0.1743 0.4064 5.020 × 10⁻⁴ 1.025 × 10⁻³ 5 0.1782 0.4080 5.105 × 10⁻⁴ 1.022 × 10⁻³ 10 0.1822 0.4095 5.189 × 10⁻⁴ 1.020 × 10⁻³ 15 0.1862 0.4111 5.273 × 10⁻⁴ 1.018 × 10⁻³ 20 0.1902 0.4126 5.357 × 10⁻⁴ 1.015 × 10⁻³ 25 0.1943 0.4142 5.440 × 10⁻⁴ 1.013 × 10⁻³ 30 0.1984 0.4156 5.523 × 10⁻⁴ 1.011 × 10⁻³ 35 0.2025 0.4171 5.605 × 10⁻⁴ 1.009 × 10⁻³ 40 0.2066 0.4185 5.687 × 10⁻⁴ 1.007 × 10⁻³ 45 0.2108 0.4199 5.769 × 10⁻⁴ 1.005 × 10⁻³ 50 0.2150 0.4213 5.850 × 10⁻⁴ 1.003 × 10⁻³ 55 0.2192 0.4226 5.931 × 10⁻⁴ 1.001 × 10⁻³ 60 0.2235 0.4239 6.012 × 10⁻⁴ 9.988 × 10⁻⁴ 65 0.2278 0.4251 6.093 × 10⁻⁴ 9.969 × 10⁻⁴ 70 0.2321 0.4263 6.174 × 10⁻⁴ 9.951 × 10⁻⁴ 75 0.2365 0.4274 6.255 × 10⁻⁴ 9.932 × 10⁻⁴ 80 0.2410 0.4285 6.335 × 10⁻⁴ 9.914 × 10⁻⁴ 85 0.2454 0.4296 6.416 × 10⁻⁴ 9.895 × 10⁻⁴ 90 0.2500 0.4306 6.497 × 10⁻⁴ 9.877 × 10⁻⁴ 95 0.2546 0.4315 6.578 × 10⁻⁴ 9.858 × 10⁻⁴ 100 0.2592 0.4323 6.659 × 10⁻⁴ 9.839 × 10⁻⁴ 105 0.2639 0.4331 6.740 × 10⁻⁴ 9.819 × 10⁻⁴ 110 0.2687 0.4338 6.822 × 10⁻⁴ 9.799 × 10⁻⁴ 115 0.2736 0.4343 6.905 × 10⁻⁴ 9.778 × 10⁻⁴ 120 0.2785 0.4348 6.987 × 10⁻⁴ 9.757 × 10⁻⁴ 125 0.2835 0.4352 7.070 × 10⁻⁴ 9.734 × 10⁻⁴

TABLE 12 Temperature, Pressure, Density, Enthalpy and Entropy Values for Example 4. Liquid Vapor Liquid Vapor Phase Phase Phase Phase Temp. Pressure Pressure Density Density (° F.) (psia) (psia) (g/cm³) (g/cm³) −60 20.70 6.950 1.354 2.136 × 10⁻³ −55 23.38 8.133 1.345 2.475 × 10⁻³ −50 26.32 9.473 1.337 2.855 × 10⁻³ −45 29.54 10.99 1.329 3.281 × 10⁻³ −40 33.06 12.69 1.320 3.755 × 10⁻³ −35 36.89 14.59 1.311 4.282 × 10⁻³ −30 41.04 16.71 1.303 4.865 × 10⁻³ −25 45.54 19.07 1.294 5.509 × 10⁻³ −20 50.40 21.69 1.285 6.219 × 10⁻³ −15 55.65 24.58 1.276 6.999 × 10⁻³ −10 61.29 27.77 1.267 7.855 × 10⁻³ −5 67.35 31.27 1.258 8.790 × 10⁻³ 0 73.85 35.11 1.249 9.812 × 10⁻³ 5 80.80 39.31 1.240 0.01093 10 88.23 43.88 1.231 0.01214 15 96.15 48.86 1.221 0.01345 20 104.6 54.27 1.211 0.01488 25 113.5 60.13 1.202 0.01642 30 123.1 66.46 1.192 0.01810 35 133.1 73.29 1.181 0.01990 40 143.8 80.66 1.171 0.02185 45 155.1 88.58 1.161 0.02395 50 167.0 97.08 1.150 0.02622 55 179.5 106.2 1.139 0.02866 60 192.7 116.0 1.128 0.03129 65 206.6 126.4 1.117 0.03412 70 221.2 137.5 1.105 0.03716 75 236.5 149.4 1.094 0.04043 80 252.6 162.1 1.082 0.04395 85 269.4 175.5 1.069 0.04774 90 286.9 189.8 1.057 0.05182 95 305.3 205.0 1.043 0.05622 100 324.5 221.1 1.030 0.06096 105 344.5 238.2 1.016 0.06607 110 365.3 256.3 1.001 0.07160 115 387.0 275.5 0.9866 0.07758 120 409.6 295.8 0.9711 0.08406 125 433.0 317.2 0.9548 0.09111 Liquid Vapor Liquid Vapor Phase Phase Phase Phase Temp. Enthalpy Enthalpy Entropy Entropy (° F.) (kJ/g) (kJ/g) (kJ/gR) (kJ/gR) −60 0.1282 0.3847 3.953 × 10⁻⁴ 1.064 × 10⁻³ −55 0.1319 0.3864 4.047 × 10⁻⁴ 1.059 × 10⁻³ −50 0.1357 0.3882 4.139 × 10⁻⁴ 1.055 × 10⁻³ −45 0.1395 0.3899 4.231 × 10⁻⁴ 1.051 × 10⁻³ −40 0.1433 0.3917 4.321 × 10⁻⁴ 1.047 × 10⁻³ −35 0.1471 0.3934 4.411 × 10⁻⁴ 1.048 × 10⁻³ −30 0.1510 0.3951 4.500 × 10⁻⁴ 1.040 × 10⁻³ −25 0.1549 0.3968 4.589 × 10⁻⁴ 1.037 × 10⁻³ −20 0.1587 0.3985 4.676 × 10⁻⁴ 1.034 × 10⁻³ −15 0.1625 0.4002 4.763 × 10⁻⁴ 1.031 × 10⁻³ −10 0.1664 0.4018 4.850 × 10⁻⁴ 1.028 × 10⁻³ −5 0.1703 0.4035 4.936 × 10⁻⁴ 1.025 × 10⁻³ 0 0.1743 0.4051 5.021 × 10⁻⁴ 1.022 × 10⁻³ 5 0.1782 0.4067 5.106 × 10⁻⁴ 1.020 × 10⁻³ 10 0.1822 0.4083 5.190 × 10⁻⁴ 1.017 × 10⁻³ 15 0.1862 0.4098 5.274 × 10⁻⁴ 1.015 × 10⁻³ 20 0.1902 0.4114 5.357 × 10⁻⁴ 1.013 × 10⁻³ 25 0.1943 0.4129 5.440 × 10⁻⁴ 1.010 × 10⁻³ 30 0.1984 0.4144 5.523 × 10⁻⁴ 1.008 × 10⁻³ 35 0.2025 0.4158 5.605 × 10⁻⁴ 1.010 × 10⁻³ 40 0.2066 0.4172 5.687 × 10⁻⁴ 1.004 × 10⁻³ 45 0.2108 0.4186 5.768 × 10⁻⁴ 1.002 × 10⁻³ 50 0.2150 0.4200 5.850 × 10⁻⁴ 1.000 × 10⁻³ 55 0.2192 0.4213 5.931 × 10⁻⁴ 9.981 × 10⁻⁴ 60 0.2235 0.4225 6.012 × 10⁻⁴ 9.962 × 10⁻⁴ 65 0.2278 0.4238 6.093 × 10⁻⁴ 9.943 × 10⁻⁴ 70 0.2321 0.4250 6.173 × 10⁻⁴ 9.925 × 10⁻⁴ 75 0.2370 0.4261 6,254 × 10⁻⁴ 9.907 × 10⁻⁴ 80 0.2409 0.4272 6.335 × 10⁻⁴ 9.888 × 10⁻⁴ 85 0.2454 0.4282 6.415 × 10⁻⁴ 9.870 × 10⁻⁴ 90 0.2500 0.4292 6.496 × 10⁻⁴ 9.851 × 10⁻⁴ 95 0.2545 0.4301 6.578 × 10⁻⁴ 9.832 × 10⁻⁴ 100 0.2592 0.4309 6.658 × 10⁻⁴ 9.813 × 10⁻⁴ 105 0.2639 0.4317 6.740 × 10⁻⁴ 9.794 × 10⁻⁴ 110 0.2690 0.4323 6.822 × 10⁻⁴ 9.773 × 10⁻⁴ 115 0.2736 0.4329 6.904 × 10⁻⁴ 9.752 × 10⁻⁴ 120 0.2785 0.4334 6.987 × 10⁻⁴ 9.731 × 10⁻⁴ 125 0.2834 0.4337 7.071 × 10⁻⁴ 9.708 × 10⁻⁴

TABLE 13 Temperature, Pressure, Density, Enthalpy and Entropy Values for Example 5. Liquid Vapor Liquid Phase Phase Phase Vapor Phase Temp. Pressure Pressure Density Density (° F.) (psia) (psia) (g/cm³) (g/cm³) −60 20.63 7.063 1.350 2.142 × 10⁻³ −55 23.31 8.264 1.342 2.481 × 10⁻³ −50 26.26 9.625 1.334 2.863 × 10⁻³ −45 29.48 11.16 1.325 3.289 × 10⁻³ −40 33.00 12.89 1.317 3.764 × 10⁻³ −35 36.83 14.82 1.308 4.291 × 10⁻³ −30 41.00 16.97 1.300 4.875 × 10⁻³ −25 45.51 19.37 1.291 5.521 × 10⁻³ −20 50.38 22.02 1.282 6.231 × 10⁻³ −15 55.64 24.96 1.273 7.012 × 10⁻³ −10 61.31 28.19 1.264 7.869 × 10⁻³ −5 67.39 31.74 1.255 8.805 × 10⁻³ 0 73.92 35.63 1.246 9.828 × 10⁻³ 5 80.80 39.89 1.237 0.0109 10 88.36 44.52 1.227 0.0122 15 96.32 49.57 1.218 0.0138 20 104.8 55.05 1.208 0.0149 25 113.8 60.98 1.198 0.0165 30 123.4 67.40 1.188 0.0181 35 133.5 74.32 1.178 0.0199 40 144.2 81.78 1.168 0.0219 45 155.6 89.80 1.158 0.0240 50 167.6 98.41 1.147 0.0263 55 180.2 107.6 1.136 0.0287 60 193.5 117.5 1.125 0.0313 65 207.5 128.1 1.114 0.0342 70 222.2 139.4 1.102 0.0372 75 237.6 151.4 1.091 0.0405 80 253.8 164.2 1.079 0.0440 85 270.7 177.8 1.066 0.0478 90 288.4 192.3 1.053 0.05187 95 307.0 207.7 1.040 0.05626 100 326.3 224.0 1.027 0.06101 105 346.5 241.2 1.013 0.06612 110 367.5 259.5 0.9985 0.07165 115 389.4 278.9 0.9835 0.07764 120 412.2 299.4 0.9680 0.08413 125 435.8 321.1 0.9517 0.09119 Liquid Vapor Liquid Vapor Phase Phase Phase Phase Temp. Enthalpy Enthalpy Entropy Entropy (° F.) (kJ/g) (kJ/g) (kJ/gR) (kJ/gR) −60 0.1279 0.3874 3.946 × 10⁻⁴ 3.919 × 10⁻⁴ −55 0.1316 0.3892 4.040 × 10⁻⁴ 4.014 × 10⁻⁴ −50 0.1354 0.3909 4.133 × 10⁻⁴ 4.109 × 10⁻⁴ −45 0.1392 0.3927 4.225 × 10⁻⁴ 4.202 × 10⁻⁴ −40 0.1431 0.3944 4.316 × 10⁻⁴ 4.294 × 10⁻⁴ −35 0.1469 0.3961 4.406 × 10⁻⁴ 4.386 × 10⁻⁴ −30 0.1507 0.3978 4.496 × 10⁻⁴ 4.477 × 10⁻⁴ −25 0.1556 0.3995 4.584 × 10⁻⁴ 4.567 × 10⁻⁴ −20 0.1585 0.4012 4.673 × 10⁻⁴ 4.657 × 10⁻⁴ −15 0.1624 0.4029 4.760 × 10⁻⁴ 4.746 × 10⁻⁴ −10 0.1663 0.4045 4.847 × 10⁻⁴ 4.834 × 10⁻⁴ −5 0.1702 0.4061 4.933 × 10⁻⁴ 4.922 × 10⁻⁴ 0 0.1742 0.4077 5.019 × 10⁻⁴ 5.009 × 10⁻⁴ 5 0.1781 0.4093 5.104 × 10⁻⁴ 5.096 × 10⁻⁴ 10 0.1821 0.4109 5.189 × 10⁻⁴ 5.182 × 10⁻⁴ 15 0.1862 0.4124 5.273 × 10⁻⁴ 5.268 × 10⁻⁴ 20 0.1902 0.4139 5.356 × 10⁻⁴ 5.353 × 10⁻⁴ 25 0.1943 0.4154 5.440 × 10⁻⁴ 5.434 × 10⁻⁴ 30 0.1984 0.4169 5.523 × 10⁻⁴ 5.522 × 10⁻⁴ 35 0.2025 0.4183 5.605 × 10⁻⁴ 5.606 × 10⁻⁴ 40 0.2066 0.4197 5.687 × 10⁻⁴ 5.690 × 10⁻⁴ 45 0.2108 0.4211 5.769 × 10⁻⁴ 5.773 × 10⁻⁴ 50 0.2150 0.4224 5.851 × 10⁻⁴ 5.857 × 10⁻⁴ 55 0.2193 0.4237 5.933 × 10⁻⁴ 5.940 × 10⁻⁴ 60 0.2236 0.4250 6.014 × 10⁻⁴ 6.023 × 10⁻⁴ 65 0.2279 0.4262 6.095 × 10⁻⁴ 6.106 × 10⁻⁴ 70 0.2323 0.4273 6.176 × 10⁻⁴ 6.189 × 10⁻⁴ 75 0.2367 0.4285 6.257 × 10⁻⁴ 6.271 × 10⁻⁴ 80 0.2411 0.4295 6.338 × 10⁻⁴ 6.354 × 10⁻⁴ 85 0.2456 0.4305 6.419 × 10⁻⁴ 6.437 × 10⁻⁴ 90 0.2502 0.4315 6.501 × 10⁻⁴ 6.520 × 10⁻⁴ 95 0.2548 0.4323 6.582 × 10⁻⁴ 6.603 × 10⁻⁴ 100 0.2595 0.4331 6.664 × 10⁻⁴ 6.687 × 10⁻⁴ 105 0.2642 0.4338 6.745 × 10⁻⁴ 6.770 × 10⁻⁴ 110 0.2690 0.4345 6.828 × 10⁻⁴ 6.855 × 10⁻⁴ 115 0.2739 0.4350 6.911 × 10⁻⁴ 6.939 × 10⁻⁴ 120 0.2790 0.4355 6.994 × 10⁻⁴ 7.025 × 10⁻⁴ 125 0.2840 0.4358 7.078 × 10⁻⁴ 7.111 × 10⁻⁴

TABLE 14 Temperature, Pressure, Density, Enthalpy and Entropy Values for Example 6. Liquid Vapor Liquid Phase Phase Phase Vapor Phase Temp. Pressure Pressure Density Density (° F.) (psia) (psia) (g/cm³) (g/cm³) −60 22.71 6.918 1.290 2.085 × 10⁻³ −55 25.56 8.098 1.282 2.417 × 10⁻³ −50 28.67 9.434 1.274 2.789 × 10⁻³ −45 32.06 10.94 1.266 3.205 × 10⁻³ −40 35.76 12.64 1.258 3.668 × 10⁻³ −35 39.77 14.54 1.250 4.184 × 10⁻³ −30 44.12 16.66 1.242 4.755 × 10⁻³ −25 48.80 19.01 1.233 5.385 × 10⁻³ −20 53.86 21.63 1.225 6.081 × 10⁻³ −15 59.30 24.52 1.216 6.844 × 10⁻³ −10 65.14 27.70 1.208 7.682 × 10⁻³ −5 71.40 31.20 1.199 8.599 × 10⁻³ 0 78.10 35.04 1.190 9.600 × 10⁻³ 5 85.26 39.23 1.181 0.01069 10 92.88 43.80 1.172 0.01188 15 101.0 48.78 1.163 0.01317 20 109.6 54.19 1.154 0.01457 25 118.8 60.04 1.144 0.01608 30 128.5 66.38 1.135 0.01772 35 138.8 73.21 1.125 0.01950 40 149.6 80.58 1.115 0.02141 45 161.0 88.50 1.105 0.02347 50 173.1 97.01 1.095 0.02570 55 185.8 106.1 1.084 0.02810 60 199.2 116.0 1.075 0.03068 65 213.1 126.3 1.063 0.03346 70 227.9 137.5 1.052 0.03645 75 243.3 149.4 1.040 0.03967 80 259.5 162.1 1.029 0.04314 85 276.4 175.5 1.017 0.04687 90 294.0 189.9 1.004 0.05089 95 312.4 205.1 0.9912 0.05522 100 331.6 221.2 0.9786 0.05990 105 351.6 238.3 0.9651 0.06495 110 372.5 256.5 0.9511 0.07041 115 394.1 275.7 0.9366 0.07632 120 416.6 296.0 0.9214 0.08275 125 440.0 317.6 0.9056 0.08974 Liquid Vapor Liquid Vapor Phase Phase Phase Phase Temp. Enthalpy Enthalpy Entropy Entropy (° F.) (kJ/g) (kJ/g) (kJ/gR) (kJ/gR) −60 0.1266 0.3845 3.919 × 10⁻⁴ 1.071 × 10⁻³ −55 0.1304 0.3863 4.014 × 10⁻⁴ 1.066 × 10⁻³ −50 0.1343 0.3881 4.109 × 10⁻⁴ 1.062 × 10⁻³ −45 0.1382 0.3899 4.202 × 10⁻⁴ 1.058 × 10⁻³ −40 0.1420 0.3917 4.294 × 10⁻⁴ 1.054 × 10⁻³ −35 0.1459 0.3935 4.399 × 10⁻⁴ 1.050 × 10⁻³ −30 0.1498 0.3953 4.480 × 10⁻⁴ 1.047 × 10⁻³ −25 0.1539 0.3971 4.567 × 10⁻⁴ 1.043 × 10⁻³ −20 0.1577 0.3988 4.657 × 10⁻⁴ 1.040 × 10⁻³ −15 0.1617 0.4006 4.746 × 10⁻⁴ 1.037 × 10⁻³ −10 0.1657 0.4023 4.834 × 10⁻⁴ 1.034 × 10⁻³ −5 0.1697 0.4040 4.922 × 10⁻⁴ 1.031 × 10⁻³ 0 0.1737 0.4057 5.009 × 10⁻⁴ 1.028 × 10⁻³ 5 0.1777 0.4074 5.096 × 10⁻⁴ 1.025 × 10⁻³ 10 0.1818 0.4090 5.182 × 10⁻⁴ 1.023 × 10⁻³ 15 0.1859 0.4106 5.267 × 10⁻⁴ 1.020 × 10⁻³ 20 0.1900 0.4122 5.353 × 10⁻⁴ 1.018 × 10⁻³ 25 0.1940 0.4138 5.437 × 10⁻⁴ 1.016 × 10⁻³ 30 0.1983 0.4153 5.522 × 10⁻⁴ 1.013 × 10⁻³ 35 0.2025 0.4168 5.606 × 10⁻⁴ 1.011 × 10⁻³ 40 0.2068 0.4183 5.690 × 10⁻⁴ 1.009 × 10⁻³ 45 0.2110 0.4197 5.773 × 10⁻⁴ 1.007 × 10⁻³ 50 0.2153 0.4212 5.857 × 10⁻⁴ 1.005 × 10⁻³ 55 0.2197 0.4225 5.940 × 10⁻⁴ 1.003 × 10⁻³ 60 0.2240 0.4239 6.023 × 10⁻⁴ 1.001 × 10⁻³ 65 0.2285 0.4252 6.106 × 10⁻⁴ 9.989 × 10⁻⁴ 70 0.2329 0.4264 6.189 × 10⁻⁴ 9.970 × 10⁻⁴ 75 0.2374 0.4276 6.271 × 10⁻⁴ 9.951 × 10⁻⁴ 80 0.2420 0.4287 6.354 × 10⁻⁴ 9.932 × 10⁻⁴ 85 0.2466 0.4298 6.437 × 10⁻⁴ 9.912 × 10⁻⁴ 90 0.2513 0.4308 6.520 × 10⁻⁴ 9.893 × 10⁻⁴ 95 0.2560 0.4318 6.603 × 10⁻⁴ 9.873 × 10⁻⁴ 100 0.2608 0.4326 6.687 × 10⁻⁴ 9.853 × 10⁻⁴ 105 0.2656 0.4334 6.770 × 10⁻⁴ 9.832 × 10⁻⁴ 110 0.2705 0.4341 6.855 × 10⁻⁴ 9.811 × 10⁻⁴ 115 0.2755 0.4347 6.939 × 10⁻⁴ 9.789 × 10⁻⁴ 120 0.2806 0.4352 7.025 × 10⁻⁴ 9.767 × 10⁻⁴ 125 0.2859 0.4356 7.111 × 10⁻⁴ 9.743 × 10⁻⁴

TABLE 15 Temperature, Pressure, Density, Enthalpy and Entropy Values for Example 7. Liquid Vapor Liquid Vapor Phase Phase Phase Phase Temp. Pressure Pressure Density Density (° F.) (psia) (psia) (g/cm3) (g/cm3) −60 20.33 6.796 1.343 2.066 × 10⁻³ −55 22.97 7.954 1.335 2.394 × 10⁻³ −50 25.87 9.266 1.327 2.762 × 10⁻³ −45 29.03 10.75 1.318 3.173 × 10⁻³ −40 32.49 12.41 1.310 3.632 × 10⁻³ −35 36.26 14.27 1.301 4.141 × 10⁻³ −30 40.34 16.35 1.293 4.710 × 10⁻³ −25 44.77 18.66 1.284 5.330 × 10⁻³ −20 49.55 21.23 1.276 6.017 × 10⁻³ −15 54.71 24.06 1.267 6.772 × 10⁻³ −10 60.27 27.18 1.258 7.510 × 10⁻³ −5 66.23 30.61 1.249 8.505 × 10⁻³ 0 72.63 34.37 1.240 9.494 × 10⁻³ 5 79.48 38.49 1.231 0.01057 10 86.79 42.97 1.222 0.01174 15 94.58 47.85 1.212 0.01302 20 102.9 53.15 1.203 0.01440 25 111.7 58.89 1.193 0.01589 30 121.1 65.10 1.183 0.01751 35 131.0 71.81 1.173 0.01923 40 141.5 79.03 1.163 0.02115 45 152.6 86.80 1.153 0.02318 50 164.3 95.14 1.143 0.02537 55 176.7 104.1 1.132 0.02774 60 189.7 113.7 1.121 0.03028 65 203.4 123.9 1.110 0.03301 70 217.8 134.8 1.099 0.03595 75 232.9 146.5 1.087 0.03912 80 248.7 158.9 1.075 0.04252 85 265.2 172.1 1.063 0.04618 90 282.6 186.2 1.051 0.05012 95 300.7 201.1 1.038 0.05437 100 319.6 216.9 1.025 0.05894 105 339.3 233.6 1.011 0.06387 110 359.8 251. 0.9969 0.06919 115 381.2 270.2 0.9823 0.07495 120 403.5 290.1 0.9671 0.08119 125 426.6 311.2 0.9513 0.08796 Liquid Vapor Liquid Vapor Phase Phase Phase Phase Temp. Enthalpy Enthalpy Entropy Entropy (° F.) (kJ/g) (kJ/g) (kJ/gR) (kJ/gR) −60 0.1277 0.3879 3.943 × 10⁻⁴ 1.072 × 10⁻³ −55 0.1315 0.3897 4.037 × 10⁻⁴ 1.068 × 10⁻³ −50 0.1353 0.3915 4.130 × 10⁻⁴ 1.063 × 10⁻³ −45 0.1391 0.3932 4.222 × 10⁻⁴ 1.059 × 10⁻³ −40 0.1430 0.3950 4.313 × 10⁻⁴ 1.055 × 10⁻³ −35 0.1468 0.3967 4.404 × 10⁻⁴ 1.052 × 10⁻³ −30 0.1507 0.3985 4.494 × 10⁻⁴ 1.005 × 10⁻³ −25 0.1545 0.4002 4.583 × 10⁻⁴ 1.045 × 10⁻³ −20 0.1584 0.4019 4.671 × 10⁻⁴ 1.041 × 10⁻³ −15 0.1623 0.4036 4.759 × 10⁻⁴ 1.038 × 10⁻³ −10 0.1662 0.4052 4.846 × 10⁻⁴ 1.035 × 10⁻³ −5 0.1702 0.4069 4.932 × 10⁻⁴ 1.032 × 10⁻³ 0 0.1741 0.4085 5.018 × 10⁻⁴ 1.030 × 10⁻³ 5 0.1781 0.4101 5.103 × 10⁻⁴ 1.027 × 10⁻³ 10 0.1821 0.4117 5.188 × 10⁻⁴ 1.025 × 10⁻³ 15 0.1861 0.4133 5.272 × 10⁻⁴ 1.022 × 10⁻³ 20 0.1902 0.4148 5.356 × 10⁻⁴ 1.020 × 10⁻³ 25 0.1943 0.4163 5.439 × 10⁻⁴ 1.018 × 10⁻³ 30 0.1984 0.4178 5.522 × 10⁻⁴ 1.015 × 10⁻³ 35 0.2025 0.4193 5.605 × 10⁻⁴ 1.013 × 10⁻³ 40 0.2066 0.4207 5.688 × 10⁻⁴ 1.011 × 10⁻³ 45 0.2108 0.4221 5.770 × 10⁻⁴ 1.009 × 10⁻³ 50 0.2150 0.4235 5.851 × 10⁻⁴ 1.007 × 10⁻³ 55 0.2193 0.4248 5.933 × 10⁻⁴ 1.005 × 10⁻³ 60 0.2236 0.4261 6.014 × 10⁻⁴ 1.003 × 10⁻³ 65 0.2279 0.4273 6.096 × 10⁻⁴ 1.001 × 10⁻³ 70 0.2323 0.4285 6.177 × 10⁻⁴ 9.994 × 10⁻⁴ 75 0.2367 0.4297 6.258 × 10⁻⁴ 9.975 × 10⁻⁴ 80 0.2411 0.4308 6.339 × 10⁻⁴ 9.957 × 10⁻⁴ 85 0.2456 0.4318 6.420 × 10⁻⁴ 9.938 × 10⁻⁴ 90 0.2502 0.4328 6.501 × 10⁻⁴ 9.919 × 10⁻⁴ 95 0.2548 0.4337 6.582 × 10⁻⁴ 9.900 × 10⁻⁴ 100 0.2595 0.4346 6.664 × 10⁻⁴ 9.881 × 10⁻⁴ 105 0.2642 0.4354 6.746 × 10⁻⁴ 9.861 × 10⁻⁴ 110 0.2690 0.4360 6.828 × 10⁻⁴ 9.841 × 10⁻⁴ 115 0.2739 0.4367 6.910 × 10⁻⁴ 9.820 × 10⁻⁴ 120 0.2788 0.4372 6.994 × 10⁻⁴ 9.800 × 10⁻⁴ 125 0.2839 0.4375 7.078 × 10⁻⁴ 9.775 × 10⁻⁴

TABLE 16 Temperature, Pressure, Density, Enthalpy and Entropy Values for Example 8. Liquid Vapor Liquid Vapor Phase Phase Phase Phase Temp. Pressure Pressure Density Density (° F.) (psia) (psia) (g/cm³) (g/cm³) −60 20.25 6.752 1.333 2.017 × 10⁻³ −55 22.89 7.903 1.325 2.336 × 10⁻³ −50 25.78 9.206 1.316 2.695 × 10⁻³ −45 28.94 10.68 1.308 3.096 × 10⁻³ −40 32.40 12.33 1.300 3.543 × 10⁻³ −35 36.16 14.18 1.292 4.039 × 10⁻³ −30 40.24 16.25 1.283 4.589 × 10⁻³ −25 44.66 18.55 1.275 5.206 × 10⁻³ −20 49.45 21.10 1.266 5.875 × 10⁻³ −15 54.61 23.92 1.258 6.600 × 10⁻³ −10 60.17 27.02 1.249 7.406 × 10⁻³ −5 66.14 30.43 1.240 8.288 × 10⁻³ 0 72.54 34.18 1.231 9.250 × 10⁻³ 5 79.39 38.27 1.222 0.01030 10 86.71 42.73 1.213 0.01144 15 94.52 47.59 1.204 0.01268 20 102.8 52.86 1.194 0.01402 25 111.7 58.58 1.185 0.01548 30 121.1 64.76 1.175 0.01705 35 131.0 71.44 1.166 0.01875 40 141.5 78.63 1.156 0.02058 45 152.7 86.36 1.145 0.02256 50 164.4 94.67 1.135 0.02469 55 176.8 103.6 1.125 0.02698 60 189.9 113.1 1.114 0.02945 65 203.6 123.3 1.103 0.03211 70 218.1 134.2 1.092 0.03496 75 233.2 145.8 1.081 0.03804 80 249.1 158.2 1.069 0.04134 85 265.7 171.4 1.057 0.04489 90 283.1 185.4 1.045 0.04869 95 301.3 200.2 1.032 0.05280 100 320.3 216.0 1.011 0.05722 105 340.2 232.7 1.006 0.06110 110 360.8 250.4 0.9924 0.06713 115 382.3 269.2 0.9781 0.07269 120 404.7 289.0 0.9633 0.07871 125 428.0 310.0 0.9477 0.08524 Liquid Vapor Liquid Vapor Phase Phase Phase Phase Temp. Enthalpy Enthalpy Entropy Entropy (° F.) (kJ/g) (kJ/g) (kJ/gR) (kJ/gR) −60 0.1251 0.3910 4.795 × 10⁻⁴ 1.173 × 10⁻³ −55 0.1290 0.3928 4.890 × 10⁻⁴ 1.168 × 10⁻³ −50 0.1328 0.3946 4.985 × 10⁻⁴ 1.164 × 10⁻³ −45 0.1367 0.3964 5.078 × 10⁻⁴ 1.159 × 10⁻³ −40 0.1406 0.3982 5.170 × 10⁻⁴ 1.155 × 10⁻³ −35 0.1445 0.3999 5.262 × 10⁻⁴ 1.152 × 10⁻³ −30 0.1484 0.4017 5.353 × 10⁻⁴ 1.148 × 10⁻³ −25 0.1523 0.4034 5.443 × 10⁻⁴ 1.144 × 10⁻³ −20 0.1562 0.4051 5.532 × 10⁻⁴ 1.141 × 10⁻³ −15 0.1602 0.4068 5.621 × 10⁻⁴ 1.138 × 10⁻³ −10 0.1642 0.4085 5.710 × 10⁻⁴ 1.135 × 10⁻³ −5 0.1681 0.4102 5.797 × 10⁻⁴ 1.132 × 10⁻³ 0 0.1721 0.4119 5.883 × 10⁻⁴ 1.129 × 10⁻³ 5 0.1762 0.4135 5.970 × 10⁻⁴ 1.126 × 10⁻³ 10 0.1802 0.4151 6.056 × 10⁻⁴ 1.124 × 10⁻³ 15 0.1843 0.4167 6.141 × 10⁻⁴ 1.121 × 10⁻³ 20 0.1884 0.4183 6.226 × 10⁻⁴ 1.119 × 10⁻³ 25 0.1925 0.4198 6.310 × 10⁻⁴ 1.116 × 10⁻³ 30 0.1966 0.4213 6.394 × 10⁻⁴ 1.114 × 10⁻³ 35 0.2008 0.4228 6.478 × 10⁻⁴ 1.112 × 10⁻³ 40 0.2050 0.4243 6.561 × 10⁻⁴ 1.109 × 10⁻³ 45 0.2093 0.4257 6.644 × 10⁻⁴ 1.107 × 10⁻³ 50 0.2135 0.4271 6.727 × 10⁻⁴ 1.105 × 10⁻³ 55 0.2178 0.4284 6.810 × 10⁻⁴ 1.103 × 10⁻³ 60 0.2222 0.4297 6.892 × 10⁻⁴ 1.101 × 10⁻³ 65 0.2265 0.4310 6.974 × 10⁻⁴ 1.099 × 10⁻³ 70 0.2310 0.4322 7.056 × 10⁻⁴ 1.097 × 10⁻³ 75 0.2354 0.4334 7.138 × 10⁻⁴ 1.095 × 10⁻³ 80 0.2399 0.4345 7.220 × 10⁻⁴ 1.094 × 10⁻³ 85 0.2445 0.4356 7.302 × 10⁻⁴ 1.092 × 10⁻³ 90 0.2491 0.4366 7.384 × 10⁻⁴ 1.090 × 10⁻³ 95 0.2537 0.4376 7.466 × 10⁻⁴ 1.088 × 10⁻³ 100 0.2584 0.4385 7.548 × 10⁻⁴ 1.086 × 10⁻³ 105 0.2632 0.4392 7.631 × 10⁻⁴ 1.084 × 10⁻³ 110 0.2681 0.4399 7.714 × 10⁻⁴ 1.082 × 10⁻³ 115 0.2730 0.4406 7.797 × 10⁻⁴ 1.080 × 10⁻³ 120 0.2780 0.4411 7.881 × 10⁻⁴ 1.077 × 10⁻³ 125 0.2831 0.4415 7.966 × 10⁻⁴ 1.075 × 10⁻³

The temperature, pressure, density, enthalpy and entropy values in Tables 9-16 compare favorably to those of R-410A, which are set forth in Table 17.

TABLE 17 Temperature, Pressure, Density, Enthalpy and Entropy Values for R-410A. Liquid Vapor Liquid Vapor Phase Phase Phase Phase Temp. Pressure Pressure Density Density (° F.) (psia) (psia) (g/cm³) (g/cm³) −60 14.95 14.89 1.349 4.225 × 10⁻³ −55 17.17 17.10 1.340 4.816 × 10⁻³ −50 19.65 19.58 1.330 5.470 × 10⁻³ −45 22.41 22.32 1.322 6.193 × 10⁻³ −40 25.45 25.36 1.313 6.989 × 10⁻³ −35 28.82 28.71 1.304 7.863 × 10⁻³ −30 32.52 32.41 1.295 8.822 × 10⁻³ −25 36.58 36.45 1.285 9.872 × 10⁻³ −20 41.03 40.89 1.276 0.01102 −15 45.88 45.72 1.267 0.01227 −10 51.17 50.99 1.257 0.01363 −5 56.91 56.71 1.247 0.01511 0 63.13 62.91 1.237 0.01671 5 69.86 69.62 1.227 0.01845 10 77.12 76.86 1.217 0.02033 15 84.95 84.66 1.207 0.02236 20 93.36 93.05 1.196 0.02460 25 102.4 102.1 1.185 0.02693 30 112.1 111.7 1.174 0.02950 35 122.4 122.0 1.163 0.03226 40 133.5 133.1 1.152 0.03524 45 145.3 144.8 1.140 0.03845 50 157.9 157.3 1.128 0.04192 55 171.2 170.7 1.116 0.04565 60 185.4 184.8 1.104 0.04969 65 200.5 199.8 1.091 0.05404 70 216.5 215.8 1.078 0.05874 75 233.4 232.6 1.064 0.06382 80 251.2 250.5 1.050 0.06933 85 270.1 269.3 1.036 0.07530 90 290.1 289.2 1.021 0.08179 95 311.1 310.2 1.005 0.08885 100 333.2 332.3 0.9889 0.09660 105 356.6 355.6 0.9719 0.1050 110 381.1 380.1 0.9540 0.1144 115 407.0 405.9 0.9352 0.1247 120 434.1 433.0 0.9152 0.1362 125 462.6 461.5 0.8937 0.1491 Liquid Vapor Liquid Vapor Phase Phase Phase Phase Temp. Enthalpy Enthalpy Entropy Entropy (° F.) (kJ/g) (kJ/g) (kJ/gR) (kJ/gR) −60 0.1268 0.3994 3.922 × 10⁻⁴ 1.075 × 10⁻³ −55 0.1306 0.4009 4.017 × 10⁻⁴ 1.070 × 10⁻³ −50 0.1345 0.4023 4.111 × 10⁻⁴ 1.065 × 10⁻³ −45 0.1383 0.4037 4.204 × 10⁻⁴ 1.061 × 10⁻³ −40 0.1422 0.4050 4.296 × 10⁻⁴ 1.056 × 10⁻³ −35 0.1460 0.4064 4.387 × 10⁻⁴ 1.052 × 10⁻³ −30 0.1499 0.4077 4.478 × 10⁻⁴ 1.048 × 10⁻³ −25 0.1538 0.4090 4.568 × 10⁻⁴ 1.044 × 10⁻³ −20 0.1577 0.4103 4.657 × 10⁻⁴ 1.040 × 10⁻³ −15 0.1617 0.4115 4.745 × 10⁻⁴ 1.036 × 10⁻³ −10 0.1657 0.4127 4.833 × 10⁻⁴ 1.033 × 10⁻³ −5 0.1696 0.4139 4.921 × 10⁻⁴ 1.029 × 10⁻³ 0 0.1737 0.4150 5.008 × 10⁻⁴ 1.026 × 10⁻³ 5 0.1777 0.4161 5.095 × 10⁻⁴ 1.023 × 10⁻³ 10 0.1818 0.4172 5.181 × 10⁻⁴ 1.019 × 10⁻³ 15 0.1858 0.4182 5.266 × 10⁻⁴ 1.016 × 10⁻³ 20 0.1900 0.4192 5.352 × 10⁻⁴ 1.013 × 10⁻³ 25 0.1941 0.4201 5.437 × 10⁻⁴ 1.010 × 10⁻³ 30 0.1983 0.4210 5.522 × 10⁻⁴ 1.007 × 10⁻³ 35 0.2025 0.4218 5.606 × 10⁻⁴ 1.004 × 10⁻³ 40 0.2068 0.4226 5.691 × 10⁻⁴ 1.001 × 10⁻³ 45 0.2111 0.4233 5.775 × 10⁻⁴ 9.981 × 10⁻⁴ 50 0.2156 0.4240 5.859 × 10⁻⁴ 9.951 × 10⁻⁴ 55 0.2200 0.4246 5.944 × 10⁻⁴ 9.922 × 10⁻⁴ 60 0.2243 0.4251 6.028 × 10⁻⁴ 9.892 × 10⁻⁴ 65 0.2288 0.4255 6.112 × 10⁻⁴ 9.862 × 10⁻⁴ 70 0.2334 0.4259 6.197 × 10⁻⁴ 9.832 × 10⁻⁴ 75 0.2380 0.4261 6.282 × 10⁻⁴ 9.801 × 10⁻⁴ 80 0.2427 0.4263 6.367 × 10⁻⁴ 9.770 × 10⁻⁴ 85 0.2475 0.4263 6.453 × 10⁻⁴ 9.737 × 10⁻⁴ 90 0.2523 0.4262 6.539 × 10⁻⁴ 9.704 × 10⁻⁴ 95 0.2573 0.4260 6.625 × 10⁻⁴ 9.669 × 10⁻⁴ 100 0.2622 0.4257 6.713 × 10⁻⁴ 9.633 × 10⁻⁴ 105 0.2674 0.4251 6.801 × 10⁻⁴ 9.596 × 10⁻⁴ 110 0.2726 0.4244 6.890 × 10⁻⁴ 9.556 × 10⁻⁴ 115 0.2780 0.4235 6.981 × 10⁻⁴ 9.513 × 10⁻⁴ 120 0.2836 0.4223 7.074 × 10⁻⁴ 9.468 × 10⁻⁴ 125 0.2893 0.4208 7.169 × 10⁻⁴ 9.418 × 10⁻⁴

The NIST REFPROP program was also used to generate the thermodynamic values for Example 15 of the disclosure and for R-404A. The results for temperature, pressure, density, enthalpy and entropy are set forth in Tables 18-19.

TABLE 18 Temperature, Pressure, Density, Enthalpy and Entropy Values for Example 15. Liquid Vapor Liquid Phase Phase Phase Vapor Phase Temp. Pressure Pressure Density Density (° F.) (psia) (psia) (g/cm³) (g/cm³) −60 13.03 5.785 1.3691 1.939 × 10⁻³ −55 14.86 6.779 1.3610 2.249 × 10⁻³ −50 16.89 7.907 1.3529 2.598 × 10⁻³ −45 19.13 9.181 1.3447 2.989 × 10⁻³ −40 21.59 10.62 1.3364 3.425 × 10⁻³ −35 24.29 12.22 1.3281 3.909 × 10⁻³ −30 27.25 14.02 1.3197 4.447 × 10⁻³ −25 30.48 16.02 1.3113 5.041 × 10⁻³ −20 34.00 18.24 1.3027 5.696 × 10⁻³ −15 37.82 20.69 1.2941 6.416 × 10⁻³ −10 41.97 23.39 1.2854 7.206 × 10⁻³ −5 46.45 26.37 1.2767 8.070 × 10⁻³ 0 51.29 29.63 1.2678 9.015 × 10⁻³ 5 56.50 33.20 1.2588 0.01005 10 62.11 37.10 1.2497 0.01117 15 68.12 41.34 1.2405 0.01238 20 74.56 45.95 1.2312 0.01370 25 81.45 50.95 1.2218 0.01513 30 88.80 56.35 1.2122 0.01668 35 96.63 62.19 1.2025 0.01835 40 105.0 68.47 1.1927 0.02015 45 113.8 75.24 1.1827 0.02210 50 123.2 82.50 1.1725 0.02419 55 133.2 90.29 1.1621 0.02645 60 143.7 98.63 1.1516 0.02887 65 154.9 107.5 1.1409 0.03148 70 166.6 117.1 1.1299 0.03428 75 179.0 127.2 1.1187 0.03729 80 192.1 138.0 1.1073 0.04053 85 205.8 149.5 1.0956 0.04400 90 220.2 161.7 1.0836 0.04774 95 235.3 174.6 1.0712 0.05175 100 251.2 188.4 1.0586 0.05607 105 267.8 202.9 1.0455 0.06072 110 285.2 218.3 1.0321 0.06572 115 303.4 234.6 1.0182 0.07112 120 322.4 251.8 1.0038 0.07695 125 342.2 269.9 0.9889 0.08326 Liquid Vapor Liquid Vapor Phase Phase Phase Phase Temp. Enthalpy Enthalpy Entropy Entropy (° F.) (kJ/g) (kJ/g) (kJ/gR) (kJ/gR) −60 0.1309 0.3737 4.009 × 10⁻⁴ 1.028 × 10⁻³ −55 0.1345 0.3755 4.100 × 10⁻⁴ 1.024 × 10⁻³ −50 0.1381 0.3773 4.189 × 10⁻⁴ 1.021 × 10⁻³ −45 0.1418 0.3791 4.277 × 10⁻⁴ 1.017 × 10⁻³ −40 0.1454 0.3808 4.365 × 10⁻⁴ 1.014 × 10⁻³ −35 0.1491 0.383 4.452 × 10⁻⁴ 1.011 × 10⁻³ −30 0.1528 0.3844 4.538 × 10⁻⁴ 1.008 × 10⁻³ −25 0.1565 0.3861 4.623 × 10⁻⁴ 1.006 × 10⁻³ −20 0.1602 0.3879 4.708 × 10⁻⁴ 1.003 × 10⁻³ −15 0.1640 0.3896 4.792 × 10⁻⁴ 1.001 × 10⁻³ −10 0.1677 0.3913 4.875 × 10⁻⁴ 9.983 × 10⁻⁴ −5 0.1715 0.3930 4.958 × 10⁻⁴ 9.961 × 10⁻⁴ 0 0.1753 0.3947 5.040 × 10⁻⁴ 9.940 × 10⁻⁴ 5 0.1791 0.3963 5.122 × 10⁻⁴ 9.920 × 10⁻⁴ 10 0.1829 0.3980 5.203 × 10⁻⁴ 9.901 × 10⁻⁴ 15 0.1866 0.3996 5.284 × 10⁻⁴ 9 883 × 10⁻⁴ 20 0.1906 0.4012 5.364 × 10⁻⁴ 9.866 × 10⁻⁴ 25 0.1945 0.4028 5.444 × 10⁻⁴ 9.849 × 10⁻⁴ 30 0.1984 0.4044 5.524 × 10⁻⁴ 9.833 × 10⁻⁴ 35 0.2024 0 4059 5.603 × 10⁻⁴ 9.818 × 10⁻⁴ 40 0.2063 0.4075 5 682 × 10⁻⁴ 9.803 × 10⁻⁴ 45 0.2103 0.4090 5.760 × 10⁻⁴ 9.789 × 10⁻⁴ 50 0.2144 0.4104 5.839 × 10⁻⁴ 9.775 × 10⁻⁴ 55 0.2184 0.4119 5.917 × 10⁻⁴ 9.762 × 10⁻⁴ 60 0.2225 0.4133 5.995 × 10⁻⁴ 9.749 × 10⁻⁴ 65 0.2266 0.4146 6.072 × 10⁻⁴ 9.736 × 10⁻⁴ 70 0.2308 0.4160 6.150 × 10⁻⁴ 9.723 × 10⁻⁴ 75 0.2351 0.4172 6.227 × 10⁻⁴ 9.711 × 10⁻⁴ 80 0.2392 0.4185 6.304 × 10⁻⁴ 9.698 × 10⁻⁴ 85 0.2435 0.4197 6.382 × 10⁻⁴ 9.686 × 10⁻⁴ 90 0.2478 0.4208 6.459 × 10⁻⁴ 9.673 × 10⁻⁴ 95 0.2522 0.4219 6.536 × 10⁻⁴ 9.660 × 10⁻⁴ 100 0.2566 0.4230 6.614 × 10⁻⁴ 9.648 × 10⁻⁴ 105 0.2611 0.4239 6.691 × 10⁻⁴ 9.634 × 10⁻⁴ 110 0.2656 0.4249 6.769 × 10⁻⁴ 9.621 × 10⁻⁴ 115 0.2702 0.4257 6.847 × 10⁻⁴ 9.607 × 10⁻⁴ 120 0.2748 0.4264 6.926 × 10⁻⁴ 9.592 × 10⁻⁴ 125 0.2796 0.4271 7.005 × 10⁻⁴ 9.577 × 10⁻⁴

TABLE 19 Temperature, Pressure, Density, Enthalpy and Entropy Values for R-404A . Liquid Vapor Liquid Phase Phase Phase Vapor Phase Temp. Pressure Pressure Density Density (° F.) (psia) (psia) (g/cm³) (g/cm³) −60 11.56 11.10 1.3212 4.212 × 10⁻³ −55 13.27 12.77 1.3127 4.805 × 10⁻³ −50 15.17 14.64 1.3042 5.462 × 10⁻³ −45 17.29 16.71 1.2956 6.186 × 10⁻³ −40 19.62 19.00 1.2869 6.984 × 10⁻³ −35 22.20 21.53 1.2782 7.861 × 10⁻³ −30 25.03 24.31 1.2693 8.822 × 10⁻³ −25 28.14 27.36 1.2604 9.872 × 10⁻³ −20 31.53 30.71 1.2514 0.01102 −15 35.23 34.35 1.2423 0.01227 −10 39.26 38.32 1.2330 0.01366 −5 43.63 42.63 1.2237 0.01510 0 48.36 47.31 1.2142 0.01670 5 53.47 52.36 1.2046 0.01843 10 58.98 57.81 1.1949 0.02030 15 64.91 63.69 1.1850 0.02232 20 71.28 70.00 1.1749 0.02450 25 78.12 76.77 1.1647 0.02686 30 85.43 84.03 1.1542 0.02940 35 93.26 91.79 1.1436 0.03213 40 101.6 100.1 1.1328 0.03508 45 110.5 108.9 1.1217 0.03825 50 120.0 118.3 1.1104 0.04166 55 130.0 128.3 1.0988 0.04534 60 140.7 138.9 1.0870 0.04931 65 152.0 150.2 1.0748 0.05358 70 164.0 162.1 1.0622 0.05819 75 176.7 174.8 1.0493 0.06317 80 190.1 188.1 1.0360 0.06855 85 204.2 202.2 1.0222 0.07438 90 219.2 217.1 1.0079 0.08070 95 234.9 232.8 0.9931 0.08758 100 251.5 249.3 0.9776 0.09507 105 268.9 266.8 0.9613 0.1033 110 287.2 285.1 0.9443 0.1123 115 306.5 304.3 0.9263 0.1222 120 326.6 324.6 0.9071 0.1333 125 348.0 345.9 0.8866 0.1456 Liquid Vapor Liquid Vapor Phase Phase Phase Phase Temp. Enthalpy Enthalpy Entropy Entropy (° F.) (kJ/g) (kJ/g) (kJ/gR) (kJ/gR) −60 0.1332 0.3368 4.064 × 10⁻⁴ 9.171 × 10⁻³ −55 0.1367 0.3385 4.150 × 10⁻⁴ 9.149 × 10⁻³ −50 0.1402 0.3402 4.235 × 10⁻⁴ 9.129 × 10⁻³ −45 0.1436 0.3419 4.320 × 10⁻⁴ 9.110 × 10⁻³ −40 0.1472 0.3435 4.403 × 10⁻⁴ 9.092 × 10⁻³ −35 0.1507 0.3452 4.487 × 10⁻⁴ 9.075 × 10⁻³ −30 0.1542 0.3468 4.569 × 10⁻⁴ 9.060 × 10⁻⁴ −25 0.1578 0.3485 4.651 × 10⁻⁴ 9.046 × 10⁻⁴ −20 0.1614 0.3501 4.733 × 10⁻⁴ 9.032 × 10⁻⁴ −15 0.1650 0.3517 4.814 × 10⁻⁴ 9.020 × 10⁻⁴ −10 0.1686 0.3533 4.894 × 10⁻⁴ 9.008 × 10⁻⁴ −5 0.1722 0.3549 4.974 × 10⁻⁴ 8.997 × 10⁻⁴ 0 0.1759 0.3564 5.054 × 10⁻⁴ 8.986 × 10⁻⁴ 5 0.1796 0.3579 5.133 × 10⁻⁴ 8.977 × 10⁻⁴ 10 0.1833 0.3595 5.212 × 10⁻⁴ 8.967 × 10⁻⁴ 15 0.1871 0.3610 5.291 × 10⁻⁴ 8.959 × 10⁻⁴ 20 0.1908 0.3624 5.369 × 10⁻⁴ 8.951 × 10⁻⁴ 25 0.1946 0.3639 5.447 × 10⁻⁴ 8 943 × 10⁻⁴ 30 0.1985 0.3653 5.525 × 10⁻⁴ 8.935 × 10⁻⁴ 35 0.2023 0.3666 5.602 × 10⁻⁴ 8.928 × 10⁻⁴ 40 0.2062 0.3680 5.679 × 10⁻⁴ 8.921 × 10⁻⁴ 45 0.2102 0.3693 5.757 × 10⁻⁴ 8.914 × 10⁻⁴ 50 0.2141 0.3706 5.834 × 10⁻⁴ 8.907 × 10⁻⁴ 55 0.2181 0.3718 5.911 × 10⁻⁴ 8.899 × 10⁻⁴ 60 0.2222 0.3730 5.988 × 10⁻⁴ 8.892 × 10⁻⁴ 65 0.2263 0.3741 6.065 × 10⁻⁴ 8 885 × 10⁻⁴ 70 0.2304 0.3752 6.142 × 10⁻⁴ 8.877 × 10⁻⁴ 75 0.2346 0.3762 6.219 × 10⁻⁴ 8.869 × 10⁻⁴ 80 0.2389 0.3771 6.297 × 10⁻⁴ 8.861 × 10⁻⁴ 85 0.2432 0.3780 6.374 × 10⁻⁴ 8.851 × 10⁻⁴ 90 0.2475 0.3788 6.452 × 10⁻⁴ 8 842 × 10⁻⁴ 95 0.2520 0.3795 6.531 × 10⁻⁴ 8.831 × 10⁻⁴ 100 0.2565 0.3800 6.610 × 10⁻⁴ 8.819 × 10⁻⁴ 105 0.2611 0.3805 6.690 × 10⁻⁴ 8.806 × 10⁻⁴ 110 0.2658 0.3809 6.770 × 10⁻⁴ 8.791 × 10⁻⁴ 115 0.2706 0.3811 6.852 × 10⁻⁴ 8.775 × 10⁻⁴ 120 0.2756 0.3811 6.935 × 10⁻⁴ 8.756 × 10⁻⁴ 125 0.2807 0.3809 7.019 × 10⁻⁴ 8.735 × 10⁻⁴

An aspect of the disclosure is that at least one component of the refrigerant formulation contains reclaimed material. The EPA defines refrigerant reclamation as a means to reprocess refrigerant to at least the purity specified in Appendix A of 40 C.F.R. § 82, subpart F (based on AHRI Standard 700-1993, Specifications for Fluorocarbon and Other Refrigerants) and to verify this purity using the analytical methodology prescribed in appendix A. The EPA requires that refrigerant be reclaimed when a certified technician recovers refrigerant and puts it in a special DOT container and has no intention of putting it back in the same system from which it was recovered.

In the disclosure, the refrigerant must be reclaimed to the AHRI Standard 700 of purity by a certified reclaimer. This requirement protects the purity of used refrigerant to prevent damage to air-conditioning and refrigeration equipment from the use of contaminated refrigerant. Equipment damage from contaminated refrigerant would result in costs to equipment owners, in releases of refrigerant from damaged equipment through increased leakage, servicing and replacement, and in reduction in consumer confidence in the quality of used refrigerant. Once the reclaimed refrigerant is brought up to standard, it can be used at least partially or wholly in the formulations of the disclosure.

Formulation with reclaimed material results in a dramatic reduction in GWP, because the reclaimed material is not being released into the atmosphere to harm the ozone layer. Compounding with up to 30% of reclaimed material results in a real GWP of 750 or less. Table 20 shows the effect on GWP for Examples 1 and 8 when formulated using reclaimed material. Boiling point values were generated using the REFPROP program.

TABLE 20 The Effect of Using Reclaimed Material on GWP. Product Ex. 1 Ex. 8 Ex. 9* Ex. 10** R-134A 15.0% 15.0% 15.0% 15.0% R-125 15.0% 15.0% 15.0% 15.0% R-32 26.0% 26.0% 26.0% 26.0% R-227ea 4.0% 4.0% 4.0% 4.0% R-152a 3.0% 0.0% 3.0% 3.0% DME 0.0% 3.0% 0.0% 0.0% CO₂ 7.0% 7.0% 7.0% 7.0% R-1234ze 30.0% 30.0% 30.0% 30.0% Total 100.0% 100.0% 100.0% 100.0% Pressure at 180.8 180.7 180.8 180.8 70° F. GWP 1048 1044 630 487 Theo. BP (° F.) −73.07 −72.44 −73.07 −73.07 *Ex. 1 using 10% reclaim content of R-410A **Ex. 1 using 10% reclaim content of R-407C (R-407C is a blend of 23 wt % R-32, 25 wt % R-125 and 52 wt % R-134a).

When using 10% reclaim content of R-410A per the proposed California language, the calculated GWP falls from 1047 to 630. When using 10% reclaim content of R-407C, the calculated GWP falls to 487.39. Accordingly, using even moderate amounts of reclaimed material has the unexpected result of reducing the GWP to a 750-400 range, a reduction of from about 29% to about 62%. This also applies to the drop-in replacements for R-404A, where the formulations for Examples 9-15 will also have a GWP of 750-400, a reduction of from about 29% to about 62%, when formulated with about 10% reclaim content.

The addition of reclaimed material will also lower the GWP of R-404A substitutes. The addition of reclaim material to formulations of Ex. 9-15 is expected to reduce the GWP to a 750-400 range.

Another issue for refrigerants is flammability. The most well established classification for this is the ASHRAE classification. Refrigerants such as R-410A, R-407A and R-404A are class 1 in their flammability, so do not show flame propagation when tested at 100° C. and 101.3 kPa in air. Class 2 refrigerants are those with flammability lower than 0.10 kg/m³ at 100° C. and 101.3 kPa and a heat of combustion of less than 19 kJ/kg. Class 3 refrigerants have flammability over this boundary and this includes many hydrocarbons.

Of the compounds used in the refrigerant formulations of the disclosure, R-227ea is a well-known fire suppressant and is governed by NFPA 2001—Standard for Clean Agent Fire Extinguishing Systems. Effective fire suppression requires introducing a concentration of the R-227ea agent between 6.25% and 9% depending on the hazard being suppressed. R-227ea has a molar mass of 170.03 g/mol, a density of 1.46 g/cm³ at 3.2° F. (−16° C.) and a boiling point of −2.5° F. (−16.4° C.).

Carbon dioxide (CO₂) is another component of the formulations of the disclosure. CO₂ is a well-known fire suppressant and is used in commercial fire extinguishers on Class B liquid fires and Class C electrical fires. The combination of R-227ea and CO₂ in the formulations of the disclosure act synergistically to enhance low flammability properties of the formulations.

CO₂ (R-744) itself acts as a refrigerant. It has a GWP of 1, a critical point of 1.067 psia at 88.0° F. and triple point of 75.1 psia at −69.9° F. CO₂ can act as a critical fluid. The phase diagram for CO₂ can be found in FIG. 12. The major challenges in CO₂ refrigeration involve the relatively high working pressures. The supercritical portion of the transcritical cycle takes place above 1,067 psia, chiefly in cascade systems for industrial and process applications. Recently, strong interest has been shown in CO₂ as a refrigerant by vending machine manufacturers. There are also possibilities for other light commercial refrigeration applications, as well as for residential air conditioning. The disclosure has unexpectedly found that CO₂ can be blended with other refrigerants to yield refrigeration power with low GWP without the need to modify refrigeration or air conditioning equipment. The refrigerants of the disclosure can thus be used as a drop-in on any equipment that uses R-410A. The refrigerants of the disclosure can also be used as the basis, with modifications, as a drop-in on equipment that used R-22, R-407C, etc.

Good performance is seen for the formulation of Example 1, which has enhanced non-flammability due to the combination of R-227ea and CO₂. For a more detailed analysis, the formulation for Example 1 compared to R-410A is in Table 21. The boiling point values were generated using REFPROP.

TABLE 21 Composition of Example 1 compared to R-410A. Chemical Name Product 410A Ex. 1 1,1,1,2- R-134a 0.00% 15.00% tetrafluoroethane pentafluoroethane R-125 50.00% 15.00% difluoromethane R-32 50.00% 26.00% 1,1,1,2,3,3,3- R-227ea 0.00% 4.00% heptafluoropropane 1,1-difluoroethane R-152a 0.00% 3.00% CO₂ CO₂ 0.00% 7.00% 1,3,3,3- R-1234ze 0.00% 30.00% tetrafluoropropene Total 100.00% 100.00% Pressure at 200.3 180.8 70° F. (psia) GWP 2088 1048 Theo BP (° F.) −60.60 −73.07

The properties of Example 1 compared to R-410A are in Table 22.

TABLE 22 Properties of Example 1 compared to R-410A at 70° F. Liquid Phase Vapor Phase Liquid Phase Vapor Phase Liquid Phase Vapor Phase Pressure Pressure Enthalpy Enthalpy Entropy Entropy Material (psia) (psia) (kJ/g) (kJ/g) (kJ/gR) (kJ/gR) Ex. 1 221.7 139.1 0.2323 0.4283 6.177 × 10⁻⁴ 9.988 × 10⁻⁴ R-410A 216.5 215.8 0.2334 0.4259 6.197 × 10⁻⁴ 9.832 × 10⁻⁴

The vapor pressure versus temperature graph for Example 1 and R-410A is shown in FIG. 13. As can be seen, the vapor pressure of Example 1 approaches that of R-410A at the lower temperatures where R-410A is usually utilized.

The liquid enthalpy of Example 1 compared to R-410A is shown in FIG. 14. As can be seen, there is a close correspondence between the formulation of Example 1 and R-410A.

The vapor enthalpy of Example 1 compared to R-410A is shown in FIG. 15. As can be seen, there is a close correspondence between the formulation of Example 1 and R-410A.

The entropy values of Example 1 compared to R-410A also have close correspondence.

Lubricants

Optionally, lubricants can be added to the formulations of the disclosure. The lubricants can be mineral oil, alkylbenzene oil or polyol ester (POE).

In another embodiment, the POE can be a synthetic POE compatible for use in refrigeration and air-conditioning compressors using HFC refrigerants, as well as for OEM retrofitting operations. The POE forms a single clear phase, i.e., is miscible with the formulations of the disclosure. Miscibility lowers the viscosity of the lubricant carried through the system, so that the lubricant can more efficiently return to the compressor. In contrast, existing mineral oil lubricants are not miscible with HFCs. The composition of the present disclosure is compatible with all types of compressors, including reciprocating and rotary in residential air conditioning, and centrifugal, reciprocating and scroll in industrial and commercial refrigeration and air conditioning.

The POE of the present disclosure can be obtained by introducing neopentyl polyol material, aliphatic monocarboxylic acid material and a catalytic quantity of acid catalyst material into a reaction zone, whereby a reaction mixture is formed, the neopentyl polyol material being at least one neopentyl polyol represented by the structural formula:

in which each R is independently selected from CH₃, C₂H₅ and CH₂OH. The aliphatic monocarboxylic acid material is at least one aliphatic hydrocarbon monocarboxylic acid, and the acid catalyst material is at least one acid esterification catalyst, wherein the initial concentration of the aliphatic monocarboxylic acid material in the reaction mixture is such as to provide an initial mole ratio of carboxyl groups to hydroxyl groups in the reaction mixture of from about 0.25:1 to about 0.5:1, and, while the reaction mixture is established and maintained at 170-200° C., aliphatic monocarboxylic acid vapor and water vapor are withdrawn from the reaction zone.

Another approach would be to produce a poly(neopentyl polyol) ester composition by (I) reacting a neopentyl polyol having the formula:

wherein each R is independently selected from the group consisting of CH₃, C₂H₅ and CH₂OH and n is a number from 1 to 4, with at least one monocarboxylic acid having 2 to 15 carbon atoms in the presence of an acid catalyst and at an initial mole ratio of carboxyl groups to hydroxyl groups of greater than 0.5:1 to 0.95:1 to form a partially esterified poly(neopentyl polyol) composition; and (ii) reacting the partially esterified poly(neopentyl polyol) composition produced in (i) with additional monocarboxylic acid having 2 to 15 Carbon atoms to form a final poly(neopentyl polyol) ester composition.

The properties of the POE of the present disclosure can be in the viscosity range of about 20 to 45 cSt at 40° C. (104° F.) and 3 to 7 cSt at 100° C. (212° F.). The viscosity index should be in the range of about 100 to 130. The pour point should be in the range of about −40 to −50° C. (−40 to −58° F.). The density at 20° C. (68° F.) should be in the range of about 0.97 to 0.98 g/ml. The flash point should be in the range of about 240 to 270° C. (464 to 518° F.). The acid value should be less than about 0.05 mg KOH/g.

The disclosure is not restricted to POE lubricant. Other lubricants can include mineral or hydrocarbon oil, alkylbenzene oil, white or paraffinic oil and mixtures thereof. The amount of lubricating oil is an amount effective to provide acceptable lubrication to the compressor parts for its longevity. An effective amount of these conventional lubricating oils is the amount recommended by the equipment manufacturer. Typically, the conventional lubricating oil is present in an amount from about 1 to about 60 wt %. The present disclosure has unexpectedly found the amount of POE to be less than about 1 wt %, as little as about 0.67 wt %, with even 0.4 wt % giving excellent lubrication. The range in which POE can be present can be from about 0.1 to about 5 wt %.

Additives

The compositions of the disclosure may also contain one or more additives such as oxidation resistance and thermal stability enhancers, corrosion inhibitors, metal deactivators, lubricity additives, viscosity index enhancers, pour and/or floc point depressants, detergents, dispersants, antifoaming agents, anti-wear agents, and extreme pressure resistant additives. Many additives are multifunctional. For example, certain additives may impart both anti-wear and extreme pressure resistance properties, or function both as a metal deactivator and a corrosion inhibitor. Cumulatively, all additives preferably do not exceed about 8 wt %, or more preferably do not exceed about 5 wt %, of the total composition.

An effective amount of the foregoing additive types is generally in the range from about 0.01 to 5 wt % for the antioxidant component, about 0.01 to 5 wt % for the corrosion inhibitor component, from about 0.001 to 0.5 wt % for the metal deactivator component, from about 0.5 to 5 wt % for the lubricity additives, from about 0.01 to 2 wt % for each of the viscosity index enhancers and pour and/or floc point depressants, from about 0.1 to 5 wt % for each of the detergents and dispersants, from about 0.001 to 0.1 wt % for antifoam agents, and from about 0.1-2 wt % for each of the anti-wear and extreme pressure resistance components. All these percentages are by weight and are based on the total composition. It is to be understood that more or less than the stated amounts of additives may be more suitable to particular circumstances, and that a single molecular type or a mixture of types may be used for each type of additive component. Also, the examples listed below are intended to be merely illustrative and not limiting.

Examples of oxidation resistance and thermal stability enhancers suitable for use in the present disclosure include, for example: diphenyl-, dinaphthyl-, and phenylnaphthyl-amines, in which the phenyl and naphthyl groups can be substituted, e.g., N,N′-diphenyl phenylenediamine, p-octyldiphenylamine, p,p-dioctyldiphenylamine, N-phenyl-1-naphthyl amine, N-phenyl-2-naphthyl amine, N-(p-dodecyl)phenyl-2-naphthyl amine, di-1-naphthylamine, and di-2-naphthylamine; phenothiazines such as N-alkyl-phenothiazines; imino(bisbenzyl); hindered phenols such as 6-(t-butyl) phenol, 2,6-di-(t-butyl) phenol, 4-methyl-2,6-di-(t-butyl) phenol, 4,4′-methylenebis(2,6-di-{t-butyl} phenol); combinations of two or more thereof, and the like.

Examples of cuprous metal deactivators suitable for use in the present disclosure include, for example: imidazole, benzamidazole, 2-mercaptobenzthiazole, 2,5-dimercaptothiadiazole, salicylidine-propylenediamine, pyrazole, benzotriazole, tolutriazole, 2-methylbenzamidazole, 3,5-dimethyl pyrazole, and methylene bis-benzotriazole. Benzotriazole derivatives are preferred. Other examples of more general metal deactivators and/or corrosion inhibitors include organic acids and their esters, metal salts, and anhydrides, e.g., N-oleyl-sarcosine, sorbitan mono-oleate, lead naphthenate, dodecenyl-succinic acid and its partial esters and amides, and 4-nonylphenoxy acetic acid; primary, secondary, and tertiary aliphatic and cycloaliphatic amines and amine salts of organic and inorganic acids, e.g., oil-soluble alkylammonium carboxylates; heterocyclic nitrogen containing compounds, e.g., thiadiazoles, substituted imidazolines, and oxazolines; quinolines, quinones, and anthraquinones; propyl gallate; barium dinonyl naphthalene sulfonate; ester and amide derivatives of alkenyl succinic anhydrides or acids, dithiocarbamates, dithiophosphates; amine salts of alkyl acid phosphates and their derivatives.

Examples of suitable lubricity additives include long chain derivatives of fatty acids and natural oils, such as esters, amines, amides, imidazolines, and borates.

Examples of suitable viscosity index enhancers include polymethacrylates, copolymers of vinyl pyrrolidone, as well as, methacrylates, polybutenes, and styrene-acrylate copolymers.

Examples of suitable pour point and/or floc point depressants include polymethacrylates such as methacrylate-ethylene-vinyl acetate terpolymers; alkylated naphthalene derivatives; and products of Friedel-Crafts catalyzed condensation of urea with naphthalene or phenols.

Examples of suitable detergents and/or dispersants include polybutenylsuccinic acid amides; polybutenyl phosphonic acid derivatives; long chain alkyl substituted aromatic sulfonic acids and their salts; and metal salts of alkyl sulfides, of alkyl phenols, and of condensation products of alkyl phenols and aldehydes.

Examples of suitable antifoam agents include silicone polymers and acrylates.

Examples of suitable anti-wear and extreme pressure resistance agents include sulfurized fatty acids and fatty acid esters, such as sulfurized octyl tallate; sulfurized terpenes; sulfurized olefins; organopolysulfides; organophosphorus derivatives including amine phosphates, alkyl acid phosphates, dialkyl phosphates, aminedithiophosphates, trialkyl and triaryl phosphorothionates, trialkyl and triaryl phosphines, and dialkylphosphites, e.g., amine salts of phosphoric acid monohexyl ester, amine salts of dinonylnaphthalene sulfonate, triphenyl phosphate, trinaphthyl phosphate, diphenyl cresyl and dicresyl phenyl phosphates, naphthyl diphenyl phosphate, triphenylphosphorothionate; dithiocarbamates, such as an antimony dialkyl dithiocarbamate; chlorinated and/or fluorinated hydrocarbons, and xanthates.

An effective amount of the foregoing additive types is generally in the range from about 0.01 to about 5 wt % for the antioxidant component, about 0.01 to about 5 wt % for the corrosion inhibitor component, from about 0.001 to about 0.5 wt % for the metal deactivator component, from about 0.5 to about 5 wt % for the lubricity additives, from about 0.01 to about 2 wt % for each of the viscosity index enhancers and pour and/or floc point depressants, from about 0.1 to about 5 wt % for each of the detergents and dispersants, from about 0.001 to about 0.1 wt % for antifoam agents, and from about 0.1 to about 2 wt % for each of the anti-wear and extreme pressure resistance components. All these percentages are by weight and are based on the total composition. It is to be understood that more or less than the stated amounts of additives may be more suitable to particular circumstances, and that a single molecular type or a mixture of types may be used for each type of additive component. As used herein, the term “effective amount” means the amount of each component which upon combination with the other component or components, results in the formation of the present compositions.

Many of the aforementioned additives are multifunctional. For example, certain additives may impart both anti-wear and extreme pressure resistance properties, or function both as a metal deactivator and a corrosion inhibitor. Cumulatively, all additives preferably do not exceed about 8% by weight, or more preferably do not exceed about 5% by weight, of the total composition.

Manufacture and Use

The refrigerant composition of the present disclosure can be used as an original OEM refrigerant or for a drop-in replacement for equipment using R-410A. The composition of the present application can also be used, with modifications, as a drop-in for HFC refrigerants such as R-22, R-404A, R-421A, R-421B, R-416A, R-417A, R-422A, R-422C, etc.

FIG. 10 is a block diagram of the manufacture of the refrigerant composition of the disclosure in a single vessel. In step 10, the vessel is charged with refrigerant components R-125, R-134a, R-32, R-227ea, R-152a and R-1234ze. Subsequently, in step 20, the appropriate amount of CO₂ is injected into the vessel to attain 100 wt % of the refrigerant composition of the disclosure.

The refrigerant composition of the disclosure can be used as a drop-in replacement for R-410A. As is shown in FIG. 11, step 30 is the selection of a substitute refrigerant formed from R-125, R-134a, R-32, R-227ea, R-152a, CO₂ and R-1234ze. Next, in step 40 the refrigerant of the disclosure is supplied under pressure to a cylinder and an R-410A compatible outlet and recharging manifold. Then, in step 50, the substitute refrigerant of the disclosure is added to the R-410A compatible apparatus.

Charging the air conditioner or refrigerator is performed using a charging cylinder designed to meter out a desired amount of a specific refrigerant by weight. Compensation for temperature variations is accomplished by reading the pressure on the gauge of the cylinder and dialing, using a calibrated chart, to the corresponding pressure reading for the refrigerant being used. When charging a refrigeration or air conditioning system with refrigerant, often the pressure in the system reaches a point where it is equal to the pressure in the charging cylinder from which the system is being charged. In order to get more refrigerant into the system to complete the charge, heat must be applied to the cylinder. In an exemplary embodiment, a standard 25 or 30 lb cylinder can be used, which is charged under pressure with the refrigerant composition of the current disclosure. This cylinder is fitted with an outlet compatible with R-410A. The outlet is connected to a recharging manifold of the apparatus to be charged.

Accordingly, the disclosure has shown that a drop-in replacement for R-410A unexpectedly produces a dramatic drop in GWP while not sacrificing performance in air conditioning systems.

Throughout the specification and the embodiments, the following terms take at least the meanings explicitly associated herein, unless the context clearly dictates otherwise. Relational terms such as “first” and “second,” and the like may be used solely to distinguish one entity or action from another entity or action without necessarily requiring or implying any actual such relationship or order between such entities or actions. The term “or” is intended to mean an inclusive “or” unless specified otherwise or clear from the context to be directed to an exclusive form. Further, the terms “a,” “an,” and “the” are intended to mean one or more unless specified otherwise or clear from the context to be directed to a singular form. The term “include” and its various forms are intended to mean including but not limited to. References to “one embodiment,” “an embodiment,” “example embodiment,” “various embodiments,” and other like terms indicate that the embodiments of the disclosed technology so described may include a particular function, feature, structure, or characteristic, but not every embodiment necessarily includes the particular function, feature, structure, or characteristic. Further, repeated use of the phrase “in one embodiment” does not necessarily refer to the same embodiment, although it may. The terms “substantially,” “essentially,” “approximately,” “about” or any other version thereof, are defined as being close to as understood by one of ordinary skill in the art, and in one non-limiting embodiment the term is defined to be within 10%, in another embodiment within 5%, in another embodiment within 1% and in another embodiment within 0.5%. A device or structure that is “configured” in a certain way is configured in at least that way, but may also be configured in ways that are not listed. 

What is claimed is:
 1. A refrigerant composition, comprising: about 18.5-20.5 wt % pentafluoroethane; about 9-11 wt % 1,1,1,2-tetrafluoroethane; about 20-22 wt % difluoromethane; about 3-5% 1,1,1,2,3,3,3-heptafluoropropane; about 2.5-4.5 wt % 1,1-difluoroethane; about 1-3 wt % CO₂; and about 39-41 wt % 1,3,3,3-tetrafluoropropene.
 2. The refrigerant composition of claim 1, wherein the refrigerant composition comprises: about 19.5 wt % pentafluoroethane; about 10 wt % 1,1,1,2-tetrafluoroethane; about 21 wt % difluoromethane; about 4 wt % 1,1,1,2,3,3,3-heptafluoropropane; about 3.5 wt % 1,1-difluoroethane; about 2 wt % CO₂; and about 40 wt % 1,3,3,3-tetrafluoropropene.
 3. The refrigerant composition of claim 1, wherein the refrigerant composition has a liquid phase pressure of about 167 psia at 70° F.
 4. The refrigerant composition of claim 1, wherein the refrigerant composition has a vapor phase pressure of about 117 psia at 70° F.
 5. The refrigerant composition of claim 1, wherein the refrigerant composition has a liquid phase enthalpy of about 0.2308 kJ/g at 70° F.
 6. The refrigerant composition of claim 1, wherein the refrigerant composition has a vapor phase enthalpy of about 0.4160 kJ/g at 70° F.
 7. The refrigerant composition of claim 1, wherein the refrigerant composition has a liquid phase entropy of about 6.150×10⁻⁴ kJ/gR at 70° F.
 8. The refrigerant composition of claim 1, wherein the refrigerant composition has a vapor phase entropy of about 9.723×10⁻⁴ kJ/gR at 70° F.
 9. The refrigerant composition of claim 1, wherein the refrigerant composition has a global warming potential of about 1000 to about
 1200. 10. The refrigerant composition of claim 1, wherein at least one of the components contains at least partially reclaimed material to yield a global warming potential of about 400-750.
 11. The refrigerant composition of claim 1, wherein the refrigerant composition contains about 10 wt % reclaimed R-404A to yield a global warming potential of about
 630. 12. A refrigerant composition having low flammability, comprising: about 18.5-20.5 wt % pentafluoroethane; about 9-11 wt % 1,1,1,2-tetrafluoroethane; about 20-22 wt % difluoromethane; about 3-5% 1,1,1,2,3,3,3-heptafluoropropane; about 2.5-4.5 wt % 1,1-difluoroethane; about 1-3 wt % CO₂; and about 39-41 wt % 1,3,3,3-tetrafluoropropene, wherein the refrigerant composition has a global warming potential of about 1000 to about
 1200. 13. The refrigerant composition of claim 12, wherein the refrigerant composition comprises: about 19.5 wt % pentafluoroethane; about 10 wt % 1,1,1,2-tetrafluoroethane; about 21 wt % difluoromethane; about 4 wt % 1,1,1,2,3,3,3-heptafluoropropane; about 3.5 wt % 1,1-difluoroethane; about 7 wt % CO₂; and about 40 wt % 1,3,3,3-tetrafluoropropene.
 14. The refrigerant composition of claim 12, wherein the refrigerant composition has a liquid phase pressure of about 167 psia at 70° F.
 15. The refrigerant composition of claim 12, wherein the refrigerant wherein the refrigerant composition has a vapor phase pressure of about 117 psia at 70° F.
 16. A refrigerant composition, comprising: about 19-21 wt % pentafluoroethane; about 7-9 wt % 1,1,1,2-tetrafluoroethane; about 21-23 wt % difluoromethane; about 3-5 wt % 1,1,1,2,3,3,3-heptafluoropropane; and about 38-40 wt % 1,3,3,3-tetrafluoropropene.
 17. The refrigerant composition of claim 16, comprising: about 20 wt % pentafluoroethane; about 8 wt % 1,1,1,2-tetrafluoroethane; about 22 wt % difluoromethane; about 4 wt % 1,1,1,2,3,3,3-heptafluoropropane; and about 39 wt % 1,3,3,3-tetrafluoropropene.
 18. The refrigerant composition of claim 16, wherein the refrigerant composition has has a liquid phase pressure of about 140 at 70° F.
 19. The refrigerant composition of claim 16, wherein the refrigerant has a global warming potential of about 1000 to about
 1200. 20. The refrigerant composition of claim 16, wherein at least one of the components contains at least partially reclaimed material to yield a global warming potential of about 400 to about
 750. 